Polypropylene Definitive

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Polypropylene The Definitive User’s Guide and Databook

Clive Maier Teresa Calafut

Plastics Design Library

Copyright 0 1998, Plastics Design Library. All rights reserved, ISBN 1-884207-58-8 Library of Congress Card Number 97-076233

Published in the United States of America, Norwich, NY by Plastics Design Library a division of William Andrew Inc. Information in this document is subject to change without notice and does not represent a commitment on the part of Plastics Design Library. No part of this document may be reproduced or transmitted in any form or by any means, electronic or mechanical, including photocopying, recording, or any information retrieval and storage system, for any purpose without the written permission of Plastics Design Library. Comments, criticisms and suggestions are invited, and should be forwarded to Plastics Design Library. Plastics Design Library and its logo are trademarks of William Andrew Inc.

Please Note: Although the information in this volume has been obtained from sources believed to be reliable, no warranty, expressed or implied, can be made as to its completeness or accuracy. Design processing methods and equipment, environment and others variables effect actual part and mechanical performance. Inasmuch as the manufacturers, suppliers and Plastics Design Library have no control over those variables or the use to which others may put the material and, therefore, cannot assume responsibility for loss or damages suffered through reliance on any information contained in this volume. No warranty is given or implied as to application and to whether there is an infringement of patents is the sole responsibility of the user. The information provided should assist in material selection and not serve as a substitute for careful testing of prototype parts in typical operating environments before beginning commercial production. Manufactured in the United States of America.

Plastics Design Library, 13 Eaton Avenue, Norwich, NY 13815 Tel: 607/337-500000 Fax: 607/337-5090

Foreword and Acknowledgements The creation of Polypropylene — The Definitive User’s Guide was a pursuit to assemble all the latest practical knowledge a technologist may need in using this versatile material. The book examines every aspect — science, technology, engineering, properties, design, processing, applications — of the continuing development and use of polypropylene. The unique treatment provided by this book means that specialists cannot only find what they want but can understand the needs and requirements of others in the product development chain. The entire work is underpinned by very extensive collections of data that allow the reader to put the information to real industrial and commercial use. As evidenced by the extensive list of sources consulted to compile this volume, the information reflects a comprehensive review of the results of current research and practical knowledge about polypropylene. The translation of the knowledge of many into a single, accessible source was accomplished by the diligent and clearheaded work of Teresa Calafut and Clive Maier. The culmination of their pursuits of excellence is evidenced in these pages. Teresa is a staff technical writer for Plastics Design Library and Clive Maier is a highly respected writer with an extensive background in plastics and is based in London, England. My gratitude for making this project happen is extended to them.

William Woishnis Editor in Chief Plastics Design Library

© Plastics Design Library

Credit for the layout and typesetting go to Jon Phipps. He accomplished the seeming impossible task of creating one fully interactive electronic version of the manuscript. Future electronic editions will be easier due to his hard work. Jeri Wachter is commended for her critique and input into the design of the book and for her neverending support. In assembling the data collections, Harold Fennel’s expertise helped make the process easier. Also deserving of special acknowledgement is Rapra Technology Ltd. and their allowing the use of Rapra Abstracts and the Plastics Knowledge Base System (KBS). For comprehensive information on the world of plastics and rubbers, these products are invaluable. The entire Plastics Design Library staff also deserves special recognition. Their continued efforts to keep our publishing activities running smoothly and profitably help ensure that volumes such as this will continue to be produced. In reviewing the manuscript, I learned many new and interesting things about polypropylene and the reasons why its use is so widespread. I also felt that I was being given the practical knowledge and rules of thumb that I wish I had available when I was using this material in previous design work. This volume is unique, is certainly a complement to previous work on the subject and is sure to provide its user years of help in making decisions and solving problems.

Introduction Polypropylene is a versatile thermoplastic material, compatible with many processing techniques and used in many different commercial applications. [797] It is one of the fastest growing classes of commodity thermoplastics, with a market share growth of 6–7%/year, and the volume of polypropylene produced is exceeded only by polyethylene and polyvinyl chloride. [794, 790] The moderate cost and favorable properties of polypropylene contribute to its strong growth rate. It is one of the lightest of all thermoplastics (0.9 g/cc), so that fewer pounds are required for finished parts. Due to its high strength-to-weight ratio, it is more rigid than other polyolefins. It has the highest melting temperature (160–170°C; 320–338°F) of all commodity thermoplastics and better heat resistance than other low-cost thermoplastics; unmodified polypropylene, however, becomes brittle at subambient temperatures. [696, 794] Its excellent chemical resistance includes resistance to most organic solvents, except for very strong oxidizing agents; however, softening may occur due to the permeation of chlorinated solvents and hydrocarbons. Its good fatigue resistance makes it widely used in “living hinge applications” — in testing, oriented thin sections can withstand more than one million repeated flexings. It is usually not susceptible to environmental stress cracking. Its clarity is greater than that of other polyolefins, and many grades can withstand commonly used sterilization methods. [696, 699] Polypropylene is available in a wide variety of melt flow rates, ranging from 0.3 to over 1000 g/10 min., and it is easily recycled. It can be processed by virtually all methods, including injection molding, blow molding, extrusion, blown and cast film, and thermoforming. [795, 794, 797, 796, 693] Many available grades with different properties make polypropylene useful in applications such as fibers, films, filaments, and injection molded parts for automobiles, rigid packaging, appliances, medical equipment, food packaging, and consumer products. It is being substituted for glass, metal, and engineering plastics such as ABS, polycarbonate, polystyrene, and nylon in kitchen appliances and large appliances such as ovens, dishwashers, refrigerators, and washing machines, and high flow grades are used in molding large housewares. Su-


per-soft grades are replacing polyvinyl chloride in medical bags and tubing and in hospital gowns. [797, 791, 793, 792, 696, 776] Polypropylene — The Definitive User’s Guide provides detailed information on the science and technology of polypropylene. The book includes chapters on the chemistry and morphology of polypropylene, common additives and fillers, and design and processing. Detailed discussions of injection molding, extrusion, blow molding, thermoforming, and fabricating polypropylene are presented in separate chapters. Descriptions of common product forms — foams, fibers, films, and sheets — are provided, in addition to commercially available forms of resins: homopolymer and random and impact copolymers. In other chapters, the many applications of polypropylene, recycling methods, and the safety and health aspects of polypropylene in use and processing are described. Properties and characteristics of polypropylene and the effect of chemistry, morphology, and processing on these characteristics are discussed. Other sections contain extensive lists of data sheet properties for representative, commonly used grades of polypropylene and an extensive compilation of data in tabular and graphical form that includes creep data, stress-strain data, fatigue, effect of UV light and weathering, effect of sterilization methods, film properties, temperature-mechanical property relationships, composition-mechanical property relationships, temperature-thermal property relationships, stress relaxation data, viscosity data, data on thermodynamic properties, and chemical and environmental stress crack resistance. Each table or graph is designed to stand alone, be easy to interpret, and provide all relevant and available details of test conditions and results. This publication serves to turn the vast amount of disparate information from wide ranging sources (i.e., conference proceedings, materials suppliers, test laboratories, monographs, and trade and technical journals) into useful engineering knowledge. Although substantial effort is exerted throughout the editorial process to maintain accuracy and consistency in presentation of information, the possibility for error exists. Often these errors occur due to insufficient or inaccurate information in the source document.

Introduction

2 How a material performs in its end use environment is a critical consideration and the information here gives useful guidelines. However, this or any other information resource should not serve as a substitute for actual testing in determining the applicability of a particular part or material in a given end use environment. Although the book contains information and data from many sources, the information is arranged to be easily accessible to readers; flexibility and ease of use were carefully considered in designing the layout of this book. It is organized so that information of interest, whether general information or detailed test data, can be quickly found, using the general index, the index of figures, the index of tables, the detailed table of contents, or the numerous sub-headings within each chapter. For readers who wish to delve beyond the

data presented, detailed source documentation is provided in the reference index; for those for whom polypropylene is a relatively new field, the glossary of terms will prove useful. We trust you will greet this reference publication with the same enthusiasm as previous Plastics Design Library titles and that it will be a useful tool in your work. As always, your feedback on improving this volume or others in the PDL Handbook series is appreciated and encouraged. Plastics Design Library 13 Eaton Avenue Norwich, NY 13815 Tel: 607-337-5080 Fax: 607-337-5090 E-mail: [email protected] Web site: www.williamandrew.com


Table of Contents Table of Contents ................................................................................................................. i Figures....................................................................................................................................... viii Graphs ....................................................................................................................................... xiv Tables ...................................................................................................................................... xviii

Introduction ......................................................................................................................... 1 1 Chemistry ....................................................................................................................... 3 1.1 1.2 1.3

Polymerization reaction .................................................................................................... 3 Stereospecificity ............................................................................................................... 3 Effect on characteristics of polypropylene ........................................................................ 4 1.3.1 1.3.2 1.3.3 1.3.4 1.3.5 1.3.6

1.4

Stereochemistry ................................................................................................................4 Molecular weight and melt flow index ...............................................................................4 Molecular weight distribution.............................................................................................5 Oxidation...........................................................................................................................6 Electrical conductivity........................................................................................................7 Chemical resistance..........................................................................................................7

Catalysts ........................................................................................................................... 7 1.4.1 1.4.2 1.4.3 1.4.4

Ziegler-Natta catalysts ......................................................................................................7 Characteristics of polypropylene produced using Ziegler-Natta catalysts.........................8 Metallocene catalysts........................................................................................................8 Characteristics of polypropylene produced using metallocene catalysts ..........................9

2 Morphology and Commercial Forms ......................................................................... 11 2.1 2.2

Crystal structure and microstructure .............................................................................. 11 Polymorphism ................................................................................................................. 12 2.2.1 2.2.2 2.2.3 2.2.4 2.2.5 2.2.6

2.3

Effect of morphology on characteristics of polypropylene .............................................. 14 2.3.1 2.3.2 2.3.3 2.3.4 2.3.5

2.4

Melting point....................................................................................................................14 Glass transition ...............................................................................................................14 Mechanical properties.....................................................................................................15 Haze................................................................................................................................15 Sterilization .....................................................................................................................15

Orientation ...................................................................................................................... 16 2.4.1 2.4.2 2.4.3 2.4.4 2.4.5

2.5

α-form of isotactic polypropylene ....................................................................................12 β-form of isotactic polypropylene ....................................................................................12 γ-form of isotactic polypropylene .....................................................................................12 Syndiotactic polypropylene .............................................................................................13 Mesomorphic polypropylene ...........................................................................................13 Amorphous polypropylene ..............................................................................................13

Fibers and films...............................................................................................................16 Effect of orientation on characteristics of fibers and films ...............................................16 Injection molding .............................................................................................................17 Effect of orientation on characteristics of injection molded parts ....................................18 Living hinges ...................................................................................................................18

Commercial Forms of Polypropylene.............................................................................. 19 2.5.1 2.5.2 2.5.3

Homopolymers................................................................................................................19 Random copolymers .......................................................................................................19 Impact copolymers..........................................................................................................21


Table of Contents

ii 2.5.4 2.5.5 2.5.6

Random block copolymers ............................................................................................. 23 Thermoplastic olefins ..................................................................................................... 23 Thermoplastic Vulcanizates ............................................................................................ 24

3 Additives .......................................................................................................................27 3.1

Antioxidants .................................................................................................................... 27 3.1.1 3.1.2 3.1.3

3.2 3.3 3.4

Acid scavengers ............................................................................................................. 29 Metal deactivators .......................................................................................................... 30 Light stabilizers............................................................................................................... 30 3.4.1 3.4.2 3.4.3 3.4.4 3.4.5 3.4.6 3.4.7

3.5 3.6

Optical effects of pigments ............................................................................................. 39 Pigment characteristics .................................................................................................. 40 Inorganic pigments ......................................................................................................... 40 Organic pigments ........................................................................................................... 41 Special effect pigments. ................................................................................................. 42 Colorant forms ................................................................................................................ 42

Antistatic agents ............................................................................................................. 44 3.8.1 3.8.2 3.8.3

3.9 3.10 3.11 3.12

Fire ................................................................................................................................. 35 Free radical scavengers ................................................................................................. 36 Magnesium hydroxide and aluminum hydroxide............................................................. 38 Phosphorus .................................................................................................................... 38 Test methods .................................................................................................................. 38

Colorants ........................................................................................................................ 39 3.7.1 3.7.2 3.7.3 3.7.4 3.7.5 3.7.6

3.8

UV absorbers ................................................................................................................. 30 Quenchers ...................................................................................................................... 32 Peroxide decomposers ................................................................................................... 32 Free radical scavengers ................................................................................................. 32 Screeners ....................................................................................................................... 34 Evaluation of UV stability................................................................................................ 34 Use of light stabilizers..................................................................................................... 34

Nucleating agents........................................................................................................... 34 Flame retardants ............................................................................................................ 35 3.6.1 3.6.2 3.6.3 3.6.4 3.6.5

3.7

Primary antioxidants....................................................................................................... 27 Secondary antioxidants .................................................................................................. 28 Antioxidant selection....................................................................................................... 29

Electrostatic charges ...................................................................................................... 44 Types of antistatic agents ............................................................................................... 44 Electrically conductive materials..................................................................................... 45

Slip agents...................................................................................................................... 45 Antiblocking agents......................................................................................................... 45 Lubricants. ...................................................................................................................... 45 Blowing or foaming agents ............................................................................................. 45 3.12.1 3.12.2 3.12.3

Physical blowing agents ................................................................................................. 45 Chemical blowing agents................................................................................................ 46 Available forms of blowing agents .................................................................................. 47

4 Fillers and reinforcements...........................................................................................49 4.1 4.2 4.3

Characteristics of fillers .................................................................................................. 49 Calcium carbonate.......................................................................................................... 50 Barite .............................................................................................................................. 51

Table of Contents


iii 4.4 4.5 4.6 4.7 4.8 4.9 4.10 4.11

Talc ................................................................................................................................. 51 Mica ................................................................................................................................ 52 Wollastonite .................................................................................................................... 53 Organic fillers.................................................................................................................. 53 Glass spheres................................................................................................................. 54 Glass fibers..................................................................................................................... 54 Carbon fibers .................................................................................................................. 55 Applications of filled polypropylene................................................................................. 55

5 Films ............................................................................................................................. 57 5.1 5.2 5.3

Unoriented film ............................................................................................................... 57 Cast film.......................................................................................................................... 57 Biaxially oriented film...................................................................................................... 57

6 Sheets ........................................................................................................................... 61 7 Fibers ............................................................................................................................ 63 7.1 7.2

Monofilaments ................................................................................................................ 63 Multifilaments.................................................................................................................. 63 7.2.1

7.3 7.4 7.5

Continuous filament and bulked continuous filament yarns ............................................64

Fiber staple..................................................................................................................... 65 Slit Tape .......................................................................................................................... 66 Spunbonded and melt-blown .......................................................................................... 66

8 Foams ........................................................................................................................... 69 8.1 8.2 8.3 8.4 8.5

General characteristics of polymeric foams.................................................................... 69 Comparison with other foamed polymers ....................................................................... 69 Polypropylene foam processing properties ..................................................................... 69 Properties of polypropylene foams ................................................................................. 70 Applications of polypropylene foams .............................................................................. 71

9 Recycling ...................................................................................................................... 75 9.1 9.2 9.3 9.4

Mechanical recycling ...................................................................................................... 76 Feedstock recycling ........................................................................................................ 77 Thermal recycling ........................................................................................................... 77 Design for recycling ........................................................................................................ 77

10 Safety and Health......................................................................................................... 79 10.1

Hazardous substances ................................................................................................... 79 10.1.1 10.1.2 10.1.3 10.1.4

10.2 10.3

Potable water .................................................................................................................. 81 Food Contact Applications.............................................................................................. 82 10.3.1 10.3.2 10.3.3

10.4

Polypropylene..................................................................................................................79 Propylene ........................................................................................................................79 VOC emissions ...............................................................................................................79 Additives..........................................................................................................................80

US food packaging regulations .......................................................................................82 Canadian food packaging regulations.............................................................................82 European food packaging regulations.............................................................................83

Medical Devices.............................................................................................................. 83


Table of Contents

iv 10.4.1 10.4.2

Migration of toxic substances ......................................................................................... 83 Regulatory guidelines..................................................................................................... 84

11 Applications..................................................................................................................87 11.1

Automotive applications.................................................................................................. 87 11.1.1 11.1.2 11.1.3

11.2 11.3

Medical Applications....................................................................................................... 92 Appliances ...................................................................................................................... 92 11.3.1 11.3.2

11.4

Floor coverings and home furnishings ........................................................................... 97 Automotive...................................................................................................................... 97 Apparel ........................................................................................................................... 97 Industrial applications and geotextiles............................................................................ 97 Non-wovens.................................................................................................................... 99

Packaging ....................................................................................................................... 99 11.5.1 11.5.2 11.5.3 11.5.4 11.5.5 11.5.6 11.5.7 11.5.8

11.6 11.7

Small appliances ............................................................................................................ 92 Large appliances ............................................................................................................ 94

Textiles and nonwovens.................................................................................................. 97 11.4.1 11.4.2 11.4.3 11.4.4 11.4.5

11.5

Exterior automotive applications..................................................................................... 87 Interior automotive applications...................................................................................... 89 Under-the-hood automotive applications........................................................................ 90

Plastics vs. other packaging materials............................................................................ 99 Use of polypropylene in packaging................................................................................. 99 High crystallinity and high melt strength grades........................................................... 100 Clarified polypropylene ................................................................................................. 100 Metallocene polypropylene........................................................................................... 100 Rigid packaging ............................................................................................................ 101 Film............................................................................................................................... 102 Barrier packaging ......................................................................................................... 103

Consumer products ...................................................................................................... 106 Building and construction ............................................................................................. 107

12 Design principles .......................................................................................................109 12.1

Design fundamentals.................................................................................................... 109 12.1.1 12.1.2

12.2

Properties influencing design ....................................................................................... 112 12.2.1 12.2.2 12.2.3 12.2.4 12.2.5 12.2.6 12.2.7 12.2.8 12.2.9 12.2.10 12.2.11 12.2.12 12.2.13

12.3

Design overview ........................................................................................................... 109 Causes of failure........................................................................................................... 111 Mechanical properties .................................................................................................. 112 Thermal properties ....................................................................................................... 120 Chemical resistance ..................................................................................................... 123 Electrical properties...................................................................................................... 124 Environmental stress cracking...................................................................................... 126 Water absorption .......................................................................................................... 127 Permeability.................................................................................................................. 127 Food and water contact ................................................................................................ 129 Sterilization................................................................................................................... 129 Transparency and optical properties ............................................................................ 131 Fire behavior................................................................................................................. 131 Weathering and light stability........................................................................................ 132 Surface properties ........................................................................................................ 134

Other factors influencing design ................................................................................... 135 12.3.1 12.3.2

Table of Contents

Orientation.................................................................................................................... 135 Distinction between homopolymer, random copolymer, block copolymer .................... 136


v 12.3.3 12.3.4

Additives........................................................................................................................137 Influence of metallocene technology.............................................................................143

13 Processing fundamentals ......................................................................................... 145 Processing overview ................................................................................................................ 145 13.1 Properties influencing processing................................................................................. 145 13.1.1 13.1.2 13.1.3

13.2

Flow properties .............................................................................................................145 Thermal properties........................................................................................................148 Shrinkage and warping .................................................................................................151

Pre-processing ............................................................................................................. 152 13.2.1 13.2.2 13.2.3

Drying ...........................................................................................................................153 Coloring.........................................................................................................................153 Safety precautions ........................................................................................................155

14 Injection molding ....................................................................................................... 159 Introduction .............................................................................................................................. 159 14.1 The process.................................................................................................................. 159 14.2 Injection molding machinery ......................................................................................... 159 14.2.1 14.2.2 14.2.3 14.2.4

14.3

Process conditions for polypropylene ........................................................................... 168 14.3.1 14.3.2 14.3.3 14.3.4 14.3.5 14.3.6

14.4

Clamp unit.....................................................................................................................159 Injection unit..................................................................................................................161 Power systems ..............................................................................................................166 Control systems ............................................................................................................167 Filling.............................................................................................................................168 Clamp............................................................................................................................170 Shrinkage and warping .................................................................................................171 Injection molding long-fiber reinforced grades ..............................................................173 Injection molding metallocene grades...........................................................................173 Trouble shooting............................................................................................................173

Injection molds.............................................................................................................. 176 14.4.1 14.4.2 14.4.3 14.4.4 14.4.5

Introduction ...................................................................................................................176 Injection Mold Components ..........................................................................................177 Injection Mold Types......................................................................................................177 Injection Mold Feed system ..........................................................................................179 Injection Mold Features.................................................................................................185

15 Blow molding ............................................................................................................. 189 Introduction .............................................................................................................................. 189 15.1 Blow molding processes ............................................................................................... 189 15.1.1 15.1.2 15.1.3 15.1.4 15.1.5 15.1.6 15.1.7 15.1.8

15.2

The extruder..................................................................................................................190 The parison head ..........................................................................................................190 Extrusion blow molding .................................................................................................192 Injection blow molding...................................................................................................194 Stretch blow molding.....................................................................................................195 Dip blow molding...........................................................................................................197 Multibloc blow molding ..................................................................................................197 Other blow molding techniques.....................................................................................198

Blow molds ................................................................................................................... 200 15.2.1 15.2.2 15.2.3

Basic features ...............................................................................................................200 Materials of construction ...............................................................................................201 Pinch-off zone ...............................................................................................................201


Table of Contents

vi 15.2.4 15.2.5 15.2.6

Blowing and calibrating devices.................................................................................... 201 Venting and surface finish............................................................................................. 202 Cooling ......................................................................................................................... 202

16 Extrusion.....................................................................................................................205 Introduction.............................................................................................................................. 205 16.1 Extrusion processes ..................................................................................................... 205 16.1.1 16.1.2 16.1.3 16.1.4 16.1.5 16.1.6 16.1.7

The extruder ................................................................................................................. 205 Film extrusion ............................................................................................................... 207 Extrusion coating.......................................................................................................... 213 Sheet extrusion............................................................................................................. 213 Fiber extrusion.............................................................................................................. 215 Pipe and tube extrusion................................................................................................ 218 Coextrusion .................................................................................................................. 221

17 Thermoforming...........................................................................................................223 Introduction.............................................................................................................................. 223 17.1 Process basics ............................................................................................................. 223 17.2 Process factors ............................................................................................................. 224 17.2.1 17.2.2 17.2.3 17.2.4 17.2.5 17.2.6

17.3

Thermoforming Processes ........................................................................................... 229 17.3.1 17.3.2 17.3.3 17.3.4 17.3.5 17.3.6 17.3.7 17.3.8 17.3.9 17.3.10 17.3.11 17.3.11 17.3.12

17.4 17.5

Forming force ............................................................................................................... 224 Mold type ...................................................................................................................... 225 Sheet pre-stretch .......................................................................................................... 226 Material input................................................................................................................ 227 Process phase.............................................................................................................. 227 Heating ......................................................................................................................... 228 Basic vacuum forming .................................................................................................. 230 Basic pressure forming................................................................................................. 230 Drape............................................................................................................................ 230 Snap back..................................................................................................................... 231 Billow ............................................................................................................................ 231 Plug assist .................................................................................................................... 231 Billow plug assist .......................................................................................................... 232 Air slip........................................................................................................................... 232 Air slip plug assist......................................................................................................... 232 Matched mold forming .................................................................................................. 232 232 Twin sheet forming........................................................................................................ 232 Trimming ....................................................................................................................... 232

Thermoforming molds .................................................................................................. 233 Thermoforming with polypropylene .............................................................................. 234

18 Fabricating and Finishing..........................................................................................237 18.1

Joining .......................................................................................................................... 237 18.1.1 18.1.2 18.1.3 18.1.4 18.1.5 18.1.6 18.1.7

Table of Contents

Heated Tool Welding ..................................................................................................... 237 Hot Gas Welding........................................................................................................... 240 Vibration welding .......................................................................................................... 241 Spin welding ................................................................................................................. 243 Ultrasonic welding ........................................................................................................ 244 Induction welding.......................................................................................................... 248 Radio Frequency Welding............................................................................................. 250


vii 18.1.8 18.1.9 18.1.10 18.1.11 18.1.12 18.1.13 18.1.14

18.2

Microwave welding ........................................................................................................250 Resistance welding .......................................................................................................251 Extrusion Welding .........................................................................................................252 Infrared Welding ............................................................................................................253 Laser Welding ...............................................................................................................254 Adhesive and solvent bonding ......................................................................................255 Mechanical Fastening ...................................................................................................261

Decorating .................................................................................................................... 265 18.2.1 18.2.2 18.2.3 18.2.4 18.2.5 18.2.6

Appliqués ......................................................................................................................265 Coloring.........................................................................................................................266 Painting .........................................................................................................................266 Metallization ..................................................................................................................266 Printing..........................................................................................................................267 Other processes............................................................................................................267

19 Polypropylene Data Collection ................................................................................. 268 19.1 19.2 19.3 19.4 19.5 19.6 19.7 19.8 19.9 19.10

Data Sheet Properties .................................................................................................. 268 Film Properties ............................................................................................................. 274 Stress vs. Strain Curves ............................................................................................... 275 Temperature-Mechanical Property Relationship........................................................... 279 Composition-Mechanical Property Relationship ........................................................... 284 Temperature-Thermal Property Relationship................................................................ 285 Creep and Stress Relaxation........................................................................................ 286 Viscosity ....................................................................................................................... 300 Thermodynamic Property ............................................................................................. 304 Fatigue.......................................................................................................................... 306 19.10.1 19.10.2 19.10.3 19.10.4

Factors Affecting Fatigue Performance .........................................................................306 Fatigue Properties.........................................................................................................307 Effect of Glass Reinforcement on Fatigue Behavior......................................................307 Effect of Molecular Weight on Fatigue Behavior............................................................308

19.11 Permeability .................................................................................................................. 316 19.11.1 Some Notes About The Information In This Section .....................................................316 19.11.2 Transport of Gases and Vapors in Barrier Materials .....................................................317 19.11.3 Permeation Coefficient and Vapor Transmission Rate ..................................................317

19.12 Effect of Weather and UV Light..................................................................................... 323 19.12.1 19.12.2 19.12.3 19.12.4

Weather Defined ...........................................................................................................323 Variations In Natural Weathering...................................................................................323 Testing For Weatherability .............................................................................................324 Effect of White Pigments on Weatherability ..................................................................324

19.13 Effect of Sterilization Methods ...................................................................................... 331 19.13.1 19.13.2 19.13.3 19.13.4 19.13.5 19.13.6 19.13.7 19.13.8

Ethylene Oxide..............................................................................................................331 Irradiation ......................................................................................................................331 Steam............................................................................................................................332 Dry Heat........................................................................................................................332 Radiation Resistance ....................................................................................................332 Gamma Radiation Resistance ......................................................................................332 Ethylene Oxide (EtO) Resistance .................................................................................334 Steam Resistance.........................................................................................................335

19.14 Chemical and Environmental Stress Crack Resistance................................................ 346


Table of Contents

viii

Glossary of Terms............................................................................................................373 Index .................................................................................................................................407 Sources.............................................................................................................................415 Supplier Directory ...........................................................................................................429

Figures Figure 1.1

Molecules of propylene and polypropylene.................................................................................. 3

Figure 1.2

Stereochemical configurations of polypropylene. ........................................................................ 4

Figure 1.3

Graph of broad and narrow molecular weight distributions in polypropylene. ............................. 5

Figure 1.4

Influence of the molecular weight distribution of a polypropylene resin on shear sensitivity. .................................................................................................................................... 6

Figure 1.5

Structure of one type of metallocene catalyst.............................................................................. 9

Figure 2.1

A Maltese cross pattern of birefringence obtained using optical microscopy under crossed polarizers. .................................................................................................................... 11

Figure 2.2

An optical micrograph showing the effect of a nucleating agent on spherulite size................... 12

Figure 2.3

Reflection optical micrograph of lamellae in isotactic polypropylene arranged in feather-like structures. ............................................................................................................... 13

Figure 2.4

A differential scanning calorimetry (DSC) melting scan of injection molded polypropylene. ........................................................................................................................... 14

Figure 2.5

Drawing of a shish-kebab structure in polypropylene. ............................................................... 17

Figure 2.6

Formation of a living hinge, shown for a fishing tackle box........................................................ 19

Figure 2.7

Random and impact copolymers, shown using ethylene as the copolymer............................... 20

Figure 2.8

The relationship between impact strength and flexural modulus of impact copolymers at –30°C (–22°F). ................................................................................................... 22

Figure 2.9

Low voltage scanning electron micrographs (LVSEM) of elastomer dispersions in polypropylene. ........................................................................................................................... 23

Figure 3.1

Stabilization reactions of primary antioxidants. ......................................................................... 27

Figure 3.2

Molecular structures of commonly used phenolic primary antioxidants. ................................... 28

Figure 3.3

Stabilization reactions of secondary antioxidants. ..................................................................... 28

Figure 3.4

Structures of phosphite antioxidants.......................................................................................... 29

Figure 3.5

Structure of 2-hydroxy-4-octoxybenzophenone, a UV absorber used in polypropylene (Uvinul 3008; BASF)........................................................................................... 31

Figure 3.6

Examples of benzotriazole UV absorbers used in polypropylene.............................................. 31

Figure 3.7

Tautomerism in ultraviolet absorbers. ........................................................................................ 31

Figure 3.8

The structure of tetramethyl piperidine, the basic structure for hindered amine light stabilizers................................................................................................................................... 32

Figure 3.9

Examples of hindered amines used as free radical scavengers in polypropylene..................... 32

Figure 3.10

The stabilization mechanism of HALS. ...................................................................................... 33

Figure 3.11

Micrograph of a spherulite of polypropylene formed in the presence of a nucleating agent.......................................................................................................................................... 34

Figure 3.12

A candle flame. .......................................................................................................................... 35

Figure 3.13

Temperature changes during stages of a fire. ........................................................................... 36

Table of Contents


ix Figure 3.14

Examples of brominated flame retardants used in polypropylene..............................................37

Figure 3.15

The UL 94 vertical burn test. ......................................................................................................39

Figure 3.16

The static decay rate of an insulating polymer and a polymer containing a conductive filler ..........................................................................................................................44

Figure 4.1

Glass fiber-filled polypropylene. .................................................................................................50

Figure 4.2

Effect of coupling on tensile strength, flexural modulus, and heat deflection temperatures of glass fiber-reinforced polypropylene. ...............................................................50

Figure 4.3

Micrographs of spherically shaped mineral fillers.......................................................................51

Figure 4.4

Micrograph of Chinese talc particles. .........................................................................................52

Figure 4.5

Micrograph of mica flakes. .........................................................................................................53

Figure 4.6

The effect of glass fiber reinforcement on mechanical properties of polypropylene. .................54

Figure 4.7

Examples of applications of reinforced polypropylene.. .............................................................56

Figure 7.1

A monofilament fiber or yarn. .....................................................................................................63

Figure 7.2

A multifilament fiber or yarn. ......................................................................................................64

Figure 7.3

Bulked continuous filament yarn. ...............................................................................................64

Figure 7.4

Staple fibers. ..............................................................................................................................66

Figure 8.1

Microstructure of a typical microcellular foamed polymer. .........................................................69

Figure 8.2

Properties of expanded polypropylene.......................................................................................70

Figure 8.3

The dynamic cushioning performance of expanded polypropylene ...........................................71

Figure 8.4

A bicycle helmet with an integral skin, molded from expanded polypropylene (BASF). ................ 72

Figure 8.5

A steering wheel molded from a blend of 60% general purpose polypropylene and 40% foamable polypropylene ..................................................................................................... 72

Figure 9.1

Recycling of post cosumer waste plastic in Europe in 1994. .....................................................75

Figure 9.2

Types of recycling.......................................................................................................................75

Figure 9.3

Diagram of the polypropylene recycling process at Hoechst. ....................................................76

Figure 11.1

Rigidity and impact strength necessary for high impact automotive applications. .....................87

Figure 11.2

Impact resistance of automobile applications at low temperatures. ...........................................87

Figure 11.3

A bumper made from talc-reinforced, elastomer-modified polypropylene ..................................88

Figure 11.4

Automotive applications for expanded polypropylene foam........................................................88

Figure 11.5

The side rubbing or protector strip on the Audi A4, produced from a polypropylene mineral-reinforced thermoplastic elastomer ...............................................................................89

Figure 11.6

Pillar trim of the Volkswagon Polo, made with 20% talc-reinforced polypropylene .....................89

Figure 11.7

Fascia on the Opel Corsa, made from 40% mineral-reinforced polypropylene ..........................90

Figure 11.8

Polypropylene door handles on the BMW 3 series ....................................................................90

Figure 11.9

Under-the-hood applications of polypropylene...........................................................................91

Figure 11.10 Various medical applications of polypropylene...........................................................................93 Figure 11.11 Applications of polypropylene in small appliances .....................................................................95 Figure 11.12 Polypropylene applications in large appliances..........................................................................96 Figure 11.13 Polypropylene applications in textiles and nonwoven fabrics. ....................................................98 Figure 11.14 Applications of polypropylene in rigid packaging......................................................................102 Figure 11.15 Applications of polypropylene films in packaging. ....................................................................104 Figure 11.16 Polypropylene applications in housewares...............................................................................105 Figure 11.17 A cordless lawnmower..............................................................................................................106 Figure 11.18 Drive wheel on the Ryobi self-propelled, battery-operated lawnmower, made from a long glass reinforced, chemically coupled polypropylene composite .......................................106 Figure 11.19 Pipe applications of polypropylene...........................................................................................107


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x Figure 12.1

Polypropylene share of world 1996 thermoplastics consumption. ........................................... 109

Figure 12.2

Unit volume cost of polypropylene compared with other thermoplastics. ................................ 109

Figure 12.3

Comparative unit volume cost of polypropylenes. ................................................................... 110

Figure 12.4

Phenomenological causes of failure in plastics articles........................................................... 111

Figure 12.5

Human causes of failure in plastics articles............................................................................. 112

Figure 12.6

Tensile behavior of polypropylene............................................................................................ 114

Figure 12.7

Temperature dependence of tensile modulus for BASF polypropylene homopolymer (Novolen 1100L), block coplymer (Novolen 2300L and Novolen 2600M), and nucleated random copolymer (Novolen 3240NC).................................................................... 115

Figure 12.8

Temperature dependence of torsional shear modulus for BASF polypropylene homopolymer (Novolen 1100L), block copolymer (Novolen 2300L and Novolen 2600M), and nucleated random copolymer (Novolen 3240NC). ............................................. 115

Figure 12.9

Temperature dependence of Charpy notched impact strength for examples of BASF polypropylene homopolymer (Novolen 1100L), block copolymer (Novolen 2300L and Novolen 2600M), and nucleated random copolymer (Novolen 3240NC). ........................ 116

Figure 12.10 Isochronous stress/strain creep plots for Hoechst Hostalen PPH 1050 polypropylene homopolymer.................................................................................................... 116 Figure 12.11 Flexural creep modulus for Hoechst Hostalen PPH 1050 polypropylene homopolymer. .......................................................................................................................... 117 Figure 12.12 Tensile creep modulus for Hoechst Hostalen PPH 1050 polypropylene homopolymer. .......................................................................................................................... 117 Figure 12.13 Tensile relaxation modulus at 23°C for Hoechst Hostalen PPH 1050 polypropylene homopolymer. .......................................................................................................................... 117 Figure 12.14 Flexural creep modulus at 23°C of Hoechst Hostacom filled and reinforced polypropylenes......................................................................................................................... 117 Figure 12.15 Flexural creep modulus at 80°C of Hoechst Hostacom filled and reinforced polypropylenes......................................................................................................................... 118 Figure 12.16 Low frequency (0.5 Hz) fatigue performance of polypropylene compared with some other semi-crystalline thermoplastics. ..................................................................................... 119 Figure 12.17 Low frequency (0.5 Hz) fatigue performance of polypropylene (semi-crystalline) compared to polycarbonate (amorphous). .............................................................................. 120 Figure 12.18 Wöhler (S-N) plot for Hoechst Hostacom M2 N01 20% talc filled polypropylene at 23°C and 10Hz. ....................................................................................................................... 120 Figure 12.19 Wöhler (S-N) plot for Hoechst Hostacom G3 N01 30% coupled glass fiber reinforced polypropylene at 23°C and 10Hz. ........................................................................... 120 Figure 12.20 Smith diagram for Hoechst Hostalen PPH 2250 polypropylene homopolymer at 23°C and 10 Hz, based on alternating tensile and compressive stress, and repeated tensile stress. ........................................................................................................... 121 Figure 12.22 Service life of polypropylene.................................................................................................... 123 Figure 12.23 The dissipation factor of polypropylene is relatively unaffected by temperature and frequency. ................................................................................................................................ 125 Figure 12.24 Temperature dependence of polypropylene to gas permeability and water vapor transmission rate. .................................................................................................................... 129 Figure 12.25 Effect of UV stabilizers on polypropylene block copolymer...................................................... 133 Figure 12.26 Flow of thermoplastics material in a channel........................................................................... 135 Figure 12.27 Variation of shear rate and orientation across the flow channel. ............................................. 136 Figure 12.28 Consumption of polypropylene types in Western Europe, 1995. ............................................. 136 Figure 12.29 Polypropylene forms compared by elongation at elastic limit as a function of flexural modulus. .................................................................................................................................. 137

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xi Figure 12.30 Polypropylene forms compared by flexural modulus as a function of tensile stress at the elastic limit..........................................................................................................................137 Figure 12.31 Polypropylene forms compared by notched Izod impact strength as a function of melt flow index..........................................................................................................................137 Figure 12.32 Polypropylene forms compared by brittleness temperature as a function of melt flow index.........................................................................................................................................137 Figure 12.33 Polypropylene forms compared by melting point as a function of flexural modulus. ................138 Figure 12.34 Polypropylene forms compared by Vicat softening point as a function of flexural modulus....................................................................................................................................138 Figure 12.35 Effect of 20% coupled and non-coupled glass fiber reinforcements on tensile strength of polypropylene. ........................................................................................................139 Figure 12.36 Effect of glass fiber reinforcement type and content on tensile strength of polypropylene. ..........................................................................................................................140 Figure 12.37 Effect of glass fiber reinforcement type and content on heat deflection temperature of polypropylene. ......................................................................................................................140 Figure 12.38 Improvement in polypropylene properties produced by long-fiber reinforcement compared with short fibers.......................................................................................................140 Figure 13.1

Processing methods for polypropylene, USA, 1996. [1216] .....................................................145

Figure 13.2

Typical viscosity curves at 260°C for some PCD polypropylene grades. .................................146

Figure 13.3

Spiral flow length of some reinforced Hoechst polypropylenes at 750 and 1130 bar injection pressure .....................................................................................................................147

Figure 13.4

Approximate relationship between melt flow index and spiral flow length. ...............................147

Figure 13.5

Comparison of broad and narrow molecular weight distributions.............................................147

Figure 13.6

Comparison of shear sensitivity for broad and narrow molecular weight distributions. .............................................................................................................................147

Figure 13.7

Effect of vis-breaking on the molecular weight distribution of polypropylene. ..........................148

Figure 13.8

Effect of vis-breaking on the melt viscosity and shear sensitivity of polypropylene..................148

Figure 13.9

Melt viscosity behavior of controlled rheology polypropylene compared with conventional polypropylene. .....................................................................................................148

Figure 13.10 Temperature dependency of specific heat of polypropylene (PP) ............................................149 Figure 13.11 Enthalpy of melt for some reinforced Hoechst polypropylenes.................................................150 Figure 13.12 PVT plot for Hoechst Hostalen PPN 1060 polypropylene homopolymer, measured during heating up. ....................................................................................................................151 Figure 13.13 Shrinkage of some particulate-reinforced Hoechst polypropylenes. ........................................152 Figure 13.14 Shrinkage of fiber-reinforced polypropylenes...........................................................................152 Figure 13.15 Typical materials safety data sheet for polypropylene. .............................................................155 Figure 14.1

Typical injection molding machine. ...........................................................................................159

Figure 14.2

Average mold pressure as a function of wall thickness for BASF Novolen1100L polypropylene homopolymer at 230°C. ....................................................................................160

Figure 14.3

Typical direct hydraulic clamp unit............................................................................................160

Figure 14.4

Typical toggle clamp unit. .........................................................................................................160

Figure 14.5

Typical reciprocating screw injection unit. ................................................................................162

Figure 14.6

Features of a typical injection screw.........................................................................................162

Figure 14.7

Material residence times. .........................................................................................................166

Figure 14.8

Example of computer-predicted pressure drops for a balanced 8-cavity mold using Pro-fax SB–823 polypropylene.................................................................................................166

Figure 14.9

Principal elements of the injection molding cycle.....................................................................167

Figure 14.10 Temperature profile for DSM Stamytec high crystallinity polypropylene...................................169


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xii Figure 14.11 Flow path length as a function of melt temperature for various grades of Hoechst Hostalen polypropylene. .......................................................................................................... 169 Figure 14.12 2mm thick flow path length as a function of specific injection pressure for various grades of Hoechst Hostalen polypropylene. ............................................................................ 170 Figure 14.13 Flow path length as a function of wall thickness for various reinforced grades of Hoechst Hostacom polypropylene ........................................................................................... 170 Figure 14.14 Flow path length as a function of wall thickness and injection pressure for talc filled grades of Hoechst Hostacom polypropylene. .......................................................................... 171 Figure 14.15 Chart for determination of clamp force. ................................................................................... 171 Figure 14.16 Shrinkage as a function of part thickness and gate area......................................................... 172 Figure 14.17 Example of injection mold illustrating principal component parts. ........................................... 176 Figure 14.18 Sequence of mold operations. ................................................................................................. 177 Figure 14.19 Schematic of 2-plate mold. ...................................................................................................... 178 Figure 14.20 Schematic of 3-plate gate. ....................................................................................................... 178 Figure 14.21 Schematic of stack mold.......................................................................................................... 178 Figure 14.22 Common runner configurations. .............................................................................................. 179 Figure 14.23 Equivalent hydraulic diameters for common runner configurations. ........................................ 179 Figure 14.24 Balanced and unbalanced runner layouts. .............................................................................. 180 Figure 14.25 Suggested approximate sprue and runner sizes. .................................................................... 180 Figure 14.26 Typical cold sprue design. ....................................................................................................... 181 Figure 14.27 Example of heated sprue bush................................................................................................ 181 Figure 14.28 Examples of various gate types............................................................................................... 182 Figure 14.29 Schematic of hot runner mold.................................................................................................. 183 Figure 14.30 Some types of direct hot runner gate. ..................................................................................... 183 Figure 14.31 Advanced hot runner gates...................................................................................................... 184 Figure 14.32 Cooling arrangements for cores of various sizes..................................................................... 186 Figure 14.33 Cooling channel considerations............................................................................................... 187 Figure 14.34 Bad and good cooling channel layouts. ................................................................................... 187 Figure 14.35 Recommended vent dimensions for use with polypropylene. .................................................. 188 Figure 15.1

Polypropylene share of Western European 1996 blow molding consumption. ........................ 189

Figure 15.2

Blow molding processes. ......................................................................................................... 190

Figure 15.3

Typical parison head................................................................................................................ 191

Figure 15.4

Principle of parison wall thickness control by axial movement of the mandrel. ....................... 192

Figure 15.5

Typical extrusion blow molding machine.................................................................................. 192

Figure 15.6

Basic extrusion blow molding process. .................................................................................... 193

Figure 15.7

Example of accumulator parison head by Bekum. .................................................................. 194

Figure 15.8

Injection blow molding stations. ............................................................................................... 194

Figure 15.9

Single-stage injection stretch blow process. ............................................................................ 196

Figure 15.10 Temperature range for stretch blow molding polypropylene. ................................................... 196 Figure 15.11 Stages in the dip blow molding process. ................................................................................. 197 Figure 15.12 Multibloc process. .................................................................................................................... 198 Figure 15.13 Typical 6-layer coextruded blow molded bottle. ....................................................................... 198 Figure 15.14 Three-layer coextrusion parison head with die profiling. ......................................................... 199 Figure 15.15 Article produced by sequential extrusion blow molding. .......................................................... 199 Figure 15.16 Stages in the blow/fill/seal process. ......................................................................................... 200 Figure 15.17 Placo process for 3D blow molding. ........................................................................................ 200

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xiii Figure 15.18 Principal features of an extrusion blow mold............................................................................201 Figure 15.19 Pinch-off zones. .......................................................................................................................201 Figure 15.20 Example of calibrating blow pin................................................................................................202 Figure 15.21 Example of blow needle. ..........................................................................................................202 Figure 16.1

Polypropylene extrusion processes, USA, 1996. .....................................................................205

Figure 16.2

Typical single-screw extruder with a vented barrel. ..................................................................206

Figure 16.3

Features of a typical extrusion screw .......................................................................................206

Figure 16.4

Mixing elements for polypropylene extrusion. ..........................................................................207

Figure 16.5

Grooved feed section of barrel. ................................................................................................207

Figure 16.6

Section of barrier screw............................................................................................................207

Figure 16.7

Typical slit die for cast film........................................................................................................208

Figure 16.8

Typical chill roll cast film line.....................................................................................................208

Figure 16.9

Detail of chill roll process. ........................................................................................................209

Figure 16.10 Typical water quench film line. .................................................................................................210 Figure 16.11 Water quench process for blown film. ......................................................................................211 Figure 16.12 Blown process for biaxially oriented film. .................................................................................212 Figure 16.13 Tenter process for biaxially oriented film. .................................................................................213 Figure 16.14 Typical sheet extrusion die. ......................................................................................................214 Figure 16.15 Three-roll sheet cooling stack. .................................................................................................214 Figure 16.16 North American fibers market 1995; market share by process. ...............................................214 Figure 16.17 Relationship between polypropylene fiber processes ..............................................................215 Figure 16.18 Fiber types and applications. ...................................................................................................215 Figure 16.19 Typical multifilament melt spinning system...............................................................................216 Figure 16.20 Typical monofilament yarn line. ................................................................................................ 217 Figure 16.21 Typical slit film tape line............................................................................................................217 Figure 16.22 Typical spun bonded fiber extrusion line. .................................................................................218 Figure 16.23 Typical spider-type tube die for pipe and tube extrusion. .........................................................219 Figure 16.24 Vacuum sizing tank used for pipe and tube extrusion. .............................................................219 Figure 16.25 Recommended relationship between pipe diameter and screw diameter. ...............................220 Figure 16.26 Creep rupture strength of pipes made from Hoechst Hostalen homopolymer (PPH 2250) and copolymer (PPH 2222) polypropylene. ...................................................................220 Figure 16.27 Schematic of coextrusion feedblock. ........................................................................................221 Figure 16.28 Three-layer multi-manifold coextrusion die...............................................................................221 Figure 17.1

Influence of plug profile on sheet thinning................................................................................226

Figure 17.2

Effect of plug pre-stretch timing on the crush resistance of cups thermoformed from Finapro PPH 4042 S polypropylene homopolymer. .................................................................227

Figure 17.3

Process phases for thermoforming polypropylene. ..................................................................228

Figure 17.4

Effect of sheet forming temperature on the crush resistance of cups thermoformed from Finapro polypropylenes....................................................................................................229

Figure 17.5

Basic vacuum forming process. [1181].....................................................................................230

Figure 17.6

Basic pressure forming process...............................................................................................230

Figure 17.7

Drape forming process. [1182] .................................................................................................230

Figure 17.8

Billow forming process. ............................................................................................................231

Figure 17.9

Basic plug assist process.........................................................................................................231

Figure 18.1

Microstructure of a hot plate weld joint.....................................................................................239


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xiv Figure 18.2

Manual hot gas welding. .......................................................................................................... 240

Figure 18.3

Linear Vibration Welding. ......................................................................................................... 241

Figure 18.4

Polarization micrographs showing microstructure of three typical vibration welds of a polypropylene homopolymer................................................................................................. 242

Figure 18.5

Microstructure of a vibration weld joint .................................................................................... 243

Figure 18.6

Spin Welding............................................................................................................................ 244

Figure 18.7

Components of an ultrasonic welder........................................................................................ 245

Figure 18.8

Ultrasonic welding using an energy director. ........................................................................... 246

Figure 18.9

A step joint with energy director............................................................................................... 248

Figure 18.10 The induction welding process. ............................................................................................... 249 Figure 18.11 Panels composed of a GMT 40% glass mat composite used to produce station wagon structural load floors..................................................................................................... 250 Figure 18.12 The resistance welding process. ............................................................................................. 251 Figure 18.13 Micrograph of a polypropylene infrared weld showing the three weld zones........................... 254 Figure 18.14 Transmitted polarized light micrograph of a polypropylene laser weld..................................... 255 Figure 18.15 The effect of plasma treatment on wettability........................................................................... 259 Figure 18.16 Common types of self-tapping screws..................................................................................... 262 Figure 18.17 A cantilever beam snap-fit. ...................................................................................................... 264 Figure 18.18 Staking..................................................................................................................................... 265

Graphs Graph 19.1

Stress vs. strain in tension for BASF AG Novolen 1100H polypropylene (melt volume index: 2.5 cc/ 10 min @ 230°C/ 2.16 kg, 4 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min....................................................275

Graph 19.2

Stress vs. strain in tension for BASF AG Novolen 1100L polypropylene (melt volume index: 7 cc/ 10 min @ 230°C/ 2.16 kg, 13 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min. ..............................................................275

Graph 19.3

Stress vs. strain in tension for BASF AG Novolen 1300L polypropylene (melt volume index: 7 cc/ 10 min @ 230°C/ 2.16 kg, 10 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min. ..............................................................276

Graph 19.4

Stress vs. strain in tension for BASF AG Novolen 1111LXGA6 PP (30% glass; melt volume index: 2.4 cc/ 10 min @ 230°C/ 2.16 kg, 5.4 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min. .....................................................276

Graph 19.5

Stress vs. strain in tension for BASF AG Novolen 1111LXGB6 polypropylene (30% glass; melt volume index: 1.6 cc/ 10 min @ 230°C/ 2.16 kg, 5.2 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min.............................................277

Graph 19.6

Stress vs. strain in tension for BASF AG Novolen 1111HXTA4 polypropylene (20% mineral; melt flow rate: 5 g/10 min.). Tested according to DIN 53455 at a strain rate of 5 mm/min..............................................................................................................................277

Graph 19.7

Stress vs. strain in tension for BASF AG Novolen 1111JXTA8 polypropylene (40% mineral; melt flow rate: 5 g/10 min.). Tested according to DIN 53455 at a strain rate of 5 mm/min..............................................................................................................................278

Graph 19.8

Stress vs. strain in tension for BASF AG Novolen 1181RCXTA2 polypropylene (10% mineral; melt volume index: 28 cc/ 10 min @ 230°C/ 2.16 kg, 52 cc/ 10 min @ 190°C/ 5 kg). Tested according to DIN 53455 at a strain rate of 5 mm/min.............................................278

Graph 19.9

Stress vs. strain in tension for Eastman Tenite 4240 polypropylene (melt flow rate: 10 g/ 10min.). Tested at a strain rate of 5.2 %/min....................................................................279

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xv Graph 19.10 Flexural modulus of elasticity vs. temperature for Phillips Marlex polypropylene. .................... 279 Graph 19.11 Flexural modulus of elasticity vs. temperature for Chisso high crystallinity polypropylene. .......................................................................................................................... 280 Graph 19.12 Flexural modulus of elasticity vs. temperature for Chisso Olehard glass/ mineral filled polypropylene................................................................................................................... 280 Graph 19.13 Tensile modulus of elasticity vs. temperature for BASF AG Novolen polypropylene. ............... 281 Graph 19.14 Shear modulus vs. temperature for BASF AG Novolen 1100RC polypropylene homopolymer............................................................................................................................ 281 Graph 19.15 Tensile strength at break vs temperature for 20% glass fiber Thermofil Polypropylene........................................................................................................................... 282 Graph 19.16 Tensile strength at break vs temperature for glass fiber/ mineral filled Chisso Olehard Polypropylene. ............................................................................................................ 282 Graph 19.17 Notched Charpy impact strength vs. temperature for BASF AG Novolen polypropylene. .......................................................................................................................... 283 Graph 19.18 Flexural modulus of elasticity vs glass fiber content for Thermofil Polypropylene. ................... 284 Graph 19.19 Tensile strength at break vs glass fiber content for Thermofil polypropylene. .......................... 284 Graph 19.20 Coefficient of thermal expansion vs. temperature for Hoechst AG Hostacom polypropylene. Measured in flow direction. .............................................................................. 285 Graph 19.21 Coefficient of thermal expansion vs. temperature for Hoechst AG Hostacom polypropylene. Measured in flow direction. .............................................................................. 285 Graph 19.22 Isochronous stress vs. strain in tension @ 23°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 286 Graph 19.23 Isochronous stress vs. strain in tension @ 40°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 286 Graph 19.24 Isochronous stress vs. strain in tension @ 100°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 287 Graph 19.25 Isochronous stress vs. strain in compression @ 23°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444................................................... 287 Graph 19.26 Isochronous stress vs. strain in compression @ 40°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444................................................... 288 Graph 19.27 Isochronous stress vs. strain in compression @ 80°C for Novolen 1100H polypropylene (homopolymer; melt volume index: 2.5 cc/10 min. @ 230°C, 2.16 kg, 4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444................................................... 288 Graph 19.28 Isochronous stress vs. strain in tension @ 23°C for Novolen 1100L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 13 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 289 Graph 19.29 Isochronous stress vs. strain in tension @ 40°C for Novolen 1100L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 13 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 289 Graph 19.30 Isochronous stress vs. strain in tension @ 100°C for Novolen 1100L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 13 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 290 Graph 19.31 Isochronous stress vs. strain in tension @ 23°C for Novolen 1300L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 10 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444....................................................................... 290


Table of Contents

xvi Graph 19.32 Isochronous stress vs. strain in tension @ 40°C for Novolen 1300L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 10 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444. ......................................................................291 Graph 19.33 Isochronous stress vs. strain in tension @ 100°C for Novolen 1300L polypropylene (homopolymer; melt volume index: 7 cc/10 min. @ 230°C, 2.16 kg, 10 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444. ......................................................................291 Graph 19.34 Isochronous stress vs. strain in tension @ 23°C for Novolen 1111LX GA6 polypropylene (30% glass fiber; melt volume index: 2.4 cc/10 min. @ 230°C, 2.16 kg, 5.4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444. .........................................292 Graph 19.35 Isochronous stress vs. strain in tension @ 40°C for Novolen 1111LX GA6 polypropylene (30% glass fiber; melt volume index: 2.4 cc/10 min. @ 230°C, 2.16 kg, 5.4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444. .........................................292 Graph 19.36 Isochronous stress vs. strain in tension @ 100°C for Novolen 1111LX GA6 polypropylene (30% glass fiber; melt volume index: 2.4 cc/10 min. @ 230°C, 2.16 kg, 5.4 cc/10 min. @190°C, 5 kg). Tested according to DIN 53444...................................................293 Graph 19.37 Isochronous stress vs. strain in tension @ 23°C for Novolen 1111HX TA4 polypropylene (20% mineral filler; melt flow: 5 g/10 min.). Tested according to DIN 53444. .....................293 Graph 19.38 Isochronous stress vs. strain in tension @ 23°C for Novolen 1111JX TA8 polypropylene (40% mineral filler; melt flow: 5 g/10 min). Tested according to DIN 53444...................294 Graph 19.39 Tensile creep strain vs time for Himont Profax polypropylene (homopolymer). ........................294 Graph 19.40 Tensile creep strain vs time for Himont Profax polypropylene copolymer. ................................295 Graph 19.41 Flexural creep strain vs time for LNF Thermocomp MF1008 40% glass reinforced polypropylene. ..........................................................................................................................295 Graph 19.42 Tensile creep modulus vs. time at 23°C for BASF AG Novolen 1100L polypropylene homopolymer. ...........................................................................................................................296 Graph 19.43 Tensile creep modulus vs. time at 40°C for BASF AG Novolen 1100L polypropylene homopolymer. ...........................................................................................................................296 Graph 19.44 Tensile creep modulus vs. time at 80°C for BASF AG Novolen 1100L polypropylene homopolymer. ...........................................................................................................................297 Graph 19.45 Tensile creep modulus vs. time at 100°C for BASF AG Novolen 1100L polypropylene homopolymer.....................................................................................................297 Graph 19.46 Tensile creep modulus vs. time at 120°C for BASF AG Novolen 1100L polypropylene homopolymer.....................................................................................................298 Graph 19.47 Tensile creep modulus vs. time at 80°C and 27.6 MPa for Himont HiGlass 40% glass fiber reinforced polypropylene. ........................................................................................298 Graph 19.48 Typical tensile creep rupture stress vs time to rupture @ 20°C for polypropylene homopolymer (source: R.Kahl, 1979, paper from Principles of Plastics Materials seminar, Center for Professional Advancement). .....................................................................299 Graph 19.49 Tensile stress relaxation modulus vs time for Hoechst AG Hostalen PPH 1050 polypropylene homopolymer.....................................................................................................299 Graph 19.50 Viscosity vs. shear rate for BASF AG Novolen 1100L polypropylene homopolymer.................300 Graph 19.51 Viscosity vs. shear rate for BASF AG Novolen 1127N polypropylene (homopolymer, film grade).................................................................................................................................300 Graph 19.52 Viscosity vs. shear rate for Hoechst AG Hostacom M2N01 20% talc filled polypropylene. ..........................................................................................................................301 Graph 19.53 Viscosity vs. shear rate for Hoechst AG Hostacom M4N01 40% talc filled polypropylene. ..........................................................................................................................301 Graph 19.54 Viscosity vs. shear rate for Hoechst AG Hostacom M1U01 10% talc filled polypropylene. ..........................................................................................................................302

Table of Contents


xvii Graph 19.55 Viscosity vs. shear rate for Hoechst AG Hostacom M2U01 20% talc filled polypropylene. .......................................................................................................................... 302 Graph 19.56 Viscosity vs. shear rate for Hoechst AG Hostacom G2N01 20% glass fiber reinforced polypropylene. ......................................................................................................... 303 Graph 19.57 Viscosity vs. shear rate for Hoechst AG Hostacom G2U02 20% glass fiber reinforced polypropylene. ......................................................................................................... 303 Graph 19.58 Viscosity vs. shear rate for Hoechst AG Hostacom G3N01 30% glass fiber reinforced polypropylene. ......................................................................................................... 304 Graph 19.59 Specific volume vs temperature for Hoechst AG Hostalen PPH 1060 polypropylene homopolymer. Measured during heating up. ............................................................................ 304 Graph 19.60 Specific heat vs temperature for polypropylene at constant pressure...................................... 305 Graph 19.61 Enthalpy vs temperature for Hoechst AG Hostacom polypropylene......................................... 305 Graph 19.62 Fatigue Cycles to Failure vs. Stress in Flexure for 50% Glass Fiber Reinforced Polypropylene with Different Molecular Weights....................................................................... 308 Graph 19.63 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostalen PPN 7180TV20 Polypropylene. ........................................................................................................ 309 Graph 19.64 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostalen PPN 7790 GV2/30 Polypropylene.............................................................................................................. 309 Graph 19.65 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostalen PPN 7790 GV2/30 Polypropylene.............................................................................................................. 310 Graph 19.66 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostacom G3N01 Polypropylene........................................................................................................................... 310 Graph 19.67 Fatigue Cycles to Failure vs. Stress in Flexure for Long Glass Fiber Reinforced Polypropylene........................................................................................................................... 311 Graph 19.68 Fatigue Cycles to Failure vs. Stress in Flexure for Long and Short Glass Fiber Reinforced Polypropylene. ....................................................................................................... 311 Graph 19.69 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostacom G3N01 Polypropylene........................................................................................................................... 312 Graph 19.70 Fatigue Cycles to Failure vs. Stress in Flexure for Hoechst Hostacom M2N01 Polypropylene........................................................................................................................... 312 Graph 19.71 Fatigue Cycles to Failure vs. Stress in Flexure for Glass Fiber Reinforced LNP Polypropylene........................................................................................................................... 313 Graph 19.72 Fatigue Cycles to Failure vs. Stress in Tension for 25% Glass Fiber Reinforced Polypropylene........................................................................................................................... 313 Graph 19.73 Fatigue Cycles to Failure vs. Stress in Tension for Long and Short Glass Reinforced Polypropylene........................................................................................................................... 314 Graph 19.74 Fatigue Cycles to Failure vs. Stress in Tension at Low Test Frequency for Polypropylene. .............. 314 Graph 19.75 Fatigue Cycles to Failure vs. Initial Strain in Tension at Different Test Frequencies for Unreinforced and 25% Glass Fiber Reinforced Polypropylene. .......................................... 315 Graph 19.76 Fatigue Cycles to Failure vs. Initial Strain in Tension at Low Test Frequency for Polypropylene........................................................................................................................... 315 Graph 19.77 Fatigue Cycles to Failure vs. Stress in Tension at Low Test Frequency for Polypropylene. .............. 316 Graph 19.78 Oxygen Permeability vs. Relative Humidity through Polypropylene. ........................................ 323 Graph 19.79 Outdoor Exposure Time vs. Chip Impact Strength of Polypropylene Copolymer ..................... 328 Graph 19.80 Outdoor Exposure Time vs. Delta E Color Change of Polypropylene Copolymer .................... 329 Graph 19.81 Outdoor Exposure Time vs. Flexural Strength of Polypropylene Copolymer............................ 329 Graph 19.82 Outdoor Exposure Time vs. Tangent Modulus of Polypropylene Copolymer ............................ 330 Graph 19.83 Outdoor Exposure Time vs. Tensile Strength of Polypropylene Copolymer.............................. 330


Table of Contents

xviii

Tables Table 1.1

Effect of Atacticity on Polypropylene Properties .......................................................................... 5

Table 1.2

Effect of Increasing Molecular Weight on Properties of Polypropylene ....................................... 5

Table 2.1

Effect of Increasing Biaxial Orientation on Properties of Polypropylene.................................... 17

Table 3.1

Comparison of Coloring Techniques.......................................................................................... 43

Table 3.2

Classifications of Surface Resistivity ......................................................................................... 44

Table 4.1

Physical Properties of Commonly Used Minerals...................................................................... 52

Table 5.1

Properties of Oriented Polypropylene Films .............................................................................. 58

Table 5.2

Properties of Novolen cast film (50 µm gauge) ......................................................................... 59

Table 6.1

Properties of Versadur Polypropylene Sheet ............................................................................. 61

Table 7.1

Useful Properties of Polypropylene in Fiber Applications .......................................................... 63

Table 7.2

Properties and Applications of Multifilaments............................................................................ 64

Table 8.1

Properties of Microfoam Extruded Foam Sheet ............................................................................ 70

Table 8.2

Permeability of Microfoam1 to Gases and Moisture ................................................................... 71

Table 8.3

Typical Mechanical Properties of Parts Made with 100% Foamable Polypropylene.................. 73

Table 8.4

Mold Shrinkage of Parts Made with Foamable Polypropylene................................................... 73

Table 10.1

Fumes Emitted during Tape Extrusion of Polypropylene (Tenax absorbent) ............................ 80

Table 10.2

Fumes Emitted during Tape Extrusion of Polypropylene (Chromosorb absorbent) ................... 80

Table 10.3

Occupational Exposure Limits (USA) for Selected Compounds................................................ 81

Table 10.4

Component migration from polypropylene into aqueous extracts.............................................. 82

Table 10.5

Some identified toxic substances in plastic medical devices ..................................................... 84

Table 10.6

Parts of ISO 10993: Biological Evaluation of Medical Devices .................................................. 84

Table 10.7

ISO 10993–1 biocompatibility tests and FDA modifications ...................................................... 85

Table 12.1

Mechanical properties of polypropylene compared with other thermoplastics. ....................... 113

Table 12.2

Mechanical properties of polypropylenes with various fillers, reinforcements, and modifiers. ................................................................................................................................. 114

Table 12.3

Common time intervals for creep testing ................................................................................. 116

Table 12.4

Dynamic low frequency (0.5 Hz) fatigue stress at 20°C and zero tension of polypropylene compared with other thermoplastics................................................................. 118

Table 12.5

Dynamic low frequency (0.5 Hz) fatigue strain at 20°C and zero tension of polypropylene compared with other thermoplastics. ............................................................... 119

Table 12.6

Suggested design safety factors for polypropylene. ................................................................ 120

Table 12.7

Thermal properties of polypropylene compared with other thermoplastics. ............................ 121

Table 12.8

Thermal properties of polypropylenes with various fillers, reinforcements and modifiers. ................................................................................................................................. 122

Table 12.9

Glass transition and crystalline melting points of polypropylene compared with other thermoplastics. ............................................................................................................... 123

Table 12.10

Thermal conductivity of polypropylene compared with other thermoplastics. ......................... 124

Table 12.11

Solubility parameters of some common plastics...................................................................... 124

Table 12.12

Effect of fillers on thermal conductivity of polypropylenes. ...................................................... 124

Table 12.13

Chemical resistance basic guide for polypropylene................................................................. 125

Table 12.14

Electrical properties of polypropylene compared with other thermoplastics. .......................... 126

Table 12.15

Electrical properties of polypropylenes with various fillers, reinforcements and modifiers. ................................................................................................................................ 127

Table 12.16

Water absorption of polypropylene compared with other thermoplastics. ............................... 128

Table of Contents


xix Table 12.17

Water absorption of polypropylenes with various fillers, reinforcements and modifiers. .............. 128

Table 12.18

Water vapor transmission of polypropylene compared with other thermoplastics.......................129

Table 12.19

Gas vapor transmission of polypropylene compared with other thermoplastics. .....................130

Table 12.20

Optical properties of polypropylene random copolymer. .........................................................131

Table 12.21

Fire behavior of polypropylene compared with other thermoplastics. ......................................132

Table 12.22

Fire behavior of polypropylenes. ..............................................................................................132

Table 12.23

Compounds produced by polypropylene at three stages of fire in low ventilation. ..................133

Table 12.24

Hardness of polypropylene compared with other thermoplastics.............................................134

Table 12.25

Dynamic coefficient of friction for polypropylene compared with other basic grades of thermoplastics...........................................................................................................................134

Table 12.26

Abrasion resistance of polypropylene compared with other thermoplastics. ..........................135

Table 12.27

Principal characteristics of polypropylene forms ......................................................................137

Table 12.28

Effect of form in fillers and reinforcements. ..............................................................................138

Table 12.29

Normal loading range for fillers and reinforcements in polypropylene......................................138

Table 12.30

Effect of polypropylene processing on reinforcing glass fibers. ..............................................140

Table 12.31

Effect of nucleation on characteristics of polypropylene. .........................................................141

Table 12.32

Comparison of conventional and metallocene polypropylenes. ..............................................143

Table 13.1

Process shear rate ranges .......................................................................................................145

Table 13.2

Approximate relationship between MFR and polypropylene injection molding conditions. ..............................................................................................................................146

Table 13.3

Approximate flow range of polypropylene compared with other thermoplastics. ....................146

Table 13.4

Principal characteristics of controlled rheology polypropylenes...............................................148

Table 13.5

Process heat requirements of polypropylene compared with other thermoplastics. .............149

Table 13.6

Approximate thermal melt properties of polypropylene compared with other thermoplastics. .........................................................................................................................150

Table 13.7

Approximate shrinkage range of polypropylene compared with other thermoplastics. .........................................................................................................................152

Table 14.1

Clamp force conversion table ................................................................................................... 161

Table 14.2

Injection pressure conversion table..........................................................................................163

Table 14.3

Shot volume conversion table ..................................................................................................164

Table 14.4

Shot weight conversion factors................................................................................................. 165

Table 14.5

Some injection molding process control factors .......................................................................167

Table 14.6

Typical barrel zone temperature settings for polypropylene. ..................................................169

Table 14.7

Melt and mold temperature ranges for polypropylene compared with other thermoplastics. .........................................................................................................................168

Table 14.8

Material factors for clamp force determination. ........................................................................171

Table 14.9

Some factors influencing polypropylene shrinkage. ................................................................172

Table 14.10

Injection molding trouble shooting chart. ................................................................................173

Table 14.11

Comparison of properties of some mold construction materials. ...........................................184

Table 14.12

Applications of principal mold steels. .....................................................................................185

Table 14.13

Recommended cooling channel dimensions for polypropylene ..............................................187

Table 16.1

Chill roll film trouble shooting chart. ........................................................................................209

Table 16.2

Influence of die and roll stack variables on sheet characteristics. ................................................ 214

Table 16.3

Suggested safe working stresses for polypropylene pipes.......................................................221

Table 17.1

Principal options available in the thermoforming process ........................................................223

Table 17.2

Principal thermoforming processes..........................................................................................224


Table of Contents

xx Table 17.3

Comparison of pressure scales for thermoforming.................................................................. 225

Table 17.4

Comparison of product characteristics between solid phase and melt phase forming..................................................................................................................................... 228

Table 17.5

Typical solid phase forming conditions for selected types of polypropylene ........................... 234

Table 18.1

Welding details and tensile results for hot plate welded isotactic pipes made from polypropylene copolymerized with ethylene ............................................................................ 239

Table 18.2

Summary of laser weld conditions and tensile properties for polypropylene joints.................. 256

Table 18.3

Adhesive systems for bonding parts made from Hostacom polypropylene ............................. 258

Table 18.4

Shear strengths of PP to PP adhesive bonds made using adhesives available from Loctite Corporation. ................................................................................................................. 261

Table 19.1

Film Properties of Coated and Uncoated Oriented Polypropylene Film .................................. 274

Table 19.2

Gas Permeability of Oxygen, Carbon Dioxide, Nitrogen and Helium Through Oriented Polypropylene Film.................................................................................................... 318

Table 19.3

Oxygen Permeability at Different Temperatures and Water Vapor Transmission Through Oriented and Non-Oriented Polypropylene. .............................................................. 318

Table 19.4

Oxygen Permeability vs. Relative Humidity Through Biaxially Oriented Polypropylene Film. ................................................................................................................. 319

Table 19.5

Water Vapor Transmission and Oxygen Permeability Through Polypropylene......................... 319

Table 19.6

Xylene and Oxygen Permeability Through Polypropylene. ...................................................... 320

Table 19.7

Water Vapor Transmission and Oxygen Permeability Through Coated and Uncoated Oriented Polypropylene Film.................................................................................................... 321

Table 19.8

Organic Solvents Permeability Through Oriented Polypropylene Film. ................................... 322

Table 19.9

d-Limonene (flavor component) Permeability Through Polypropylene..................................... 322

Table 19.10

Effect of Antioxidants on Outdoor Weathering in Florida and Puerto Rico of Polypropylene. ......................................................................................................................... 325

Table 19.11

Outdoor Weathering in California and Pennsylvania of Glass Reinforced Polypropylene. ......................................................................................................................... 326

Table 19.12

Effect of Stabilizers and Antioxidants on Outdoor Weathering in Puerto Rico of Polypropylene. ......................................................................................................................... 327

Table 19.13

Effect of ECC International Microcal Calcium Carbonate on Accelerated Weathering in QUV of Polypropylene. ..................................................................................... 328

Table 19.14

Effect of Gamma Radiation Sterilization on Polypropylene ..................................................... 335

Table 19.15


Table 19.16


Table 19.17


Table 19.18


Table 19.19


Table 19.20


Table 19.21


Table 19.22


Table 19.23


Table 19.24


Table 19.25


Table 19.26


Table 19.27


Table 19.28

Effect of Ethylene Oxide Sterilization on Polypropylene .......................................................... 344

Table 19.29

Effect of Ethylene Oxide Sterilization on Polypropylene .......................................................... 345

Table of Contents


1 1.1

Chemistry

Polymerization reaction

Polypropylene is prepared by polymerizing propylene, a gaseous byproduct of petroleum refining, in the presence of a catalyst under carefully controlled heat and pressure. [773] Propylene is an unsaturated hydrocarbon, containing only carbon and hydrogen atoms: CH2 = CH  CH3 Propylene

In the polymerization reaction, many propylene molecules (monomers) are joined together to form one large molecule of polypropylene. Propylene is reacted with an organometallic, transition metal catalyst (see 1.4 Catalysts for a description of catalysts used in the reaction) to provide a site for the reaction to occur, and propylene molecules are added sequentially through a reaction between the metallic functional group on the growing polymer chain and the unsaturated bond of the propylene monomer: M* + CH2 =CH →  CH3 M −CH2CH2 + CH2 =CH →   CH3 CH3 M −CH2CHCH2CH2 → etc.   CH3 CH3

One of the double-bonded carbon atoms of the incoming propylene molecule inserts itself into the bond between the metal catalyst (M in the above reaction) and the last carbon atom of the polypropylene chain. A long, linear polymer chain of carbon atoms is formed, with methyl (CH3) groups attached to every other carbon atom of the chain (Figure 1.1). Thousands of propylene molecules can be added sequentially until the chain reaction is terminated. [764, 768]

1.2

Stereospecificity

With Ziegler-Natta or metallocene catalysts, the polymerization reaction is highly stereospecific. Propylene molecules add to the polymer chain only in a particular orientation, depending on the chemi-


Figure 1.1 Molecules of propylene and polypropylene. In the polymerization reaction, propylene monomers (top) are added sequentially to the growing polymer chain (bottom), to form a long, linear polymer chain composed of thousands of propylene monomers. The portion of the chain shown in parentheses is repeated n number of times to form the polymer. [642]

cal and crystal structure of the catalyst, and a regular, repeating three-dimensional structure is produced in the polymer chain [763]. Propylene molecules are added to the main polymer chain, increasing the chain length, and not to one of the methyl groups attached to alternating carbon atoms (the pendant methyl groups), which would result in branching. Propylene molecules are usually added head-to-tail and not tail-to-tail or head-to-head. Head-to-tail addition results in a polypropylene chain with pendant methyl groups attached to alternating carbons; in tail-to-tail or head-to head addition, this alternating arrangement is disrupted. [771] CH2 =CH* + −CH2 −CH −CH2 −CH − →    CH3 CH3 CH3 −CH2 −CH −CH2 −CH −CH2 −CH −    CH3 CH3 CH3 Head-to-tail addition of propylene to the growing polypropylene chain CH2 =CH* + −CH2 −CH −CH2 −CH − →    CH3 CH3 CH3 −CH2 −CH −CH2 −CH −CH2 −CH −    CH3 CH3 CH3 Tail-to-tail addition of propylene to the growing polypropylene chain

Chemistry

4 same side of the polypropylene chain, as in isotactic polypropylene; however, other methyl groups are inserted at regular intervals on the opposite side of the chain. [794, 695, 810]

1.3

Effect on characteristics of polypropylene

The structure and stereochemistry of polypropylene affect its properties.

Figure 1.2 Stereochemical configurations of polypropylene. In isotactic polypropylene, top, the pendant methyl groups branching off from the polymer backbone are all on the same side of the polymer backbone, with identical configurations relative to the main chain. In syndiotactic polypropylene, middle, consecutive pendant methyl groups are on opposite sides of the polymer backbone chain. In atactic polypropylene, bottom, pendant methyl groups are oriented randomly with respect to the polymer backbone. The portion of the chain shown is repeated n number of times to form the polymer. [642]

Occasional tail-to-tail or head-to-tail additions of polypropylene to the growing polymer chain disrupt the crystalline structure and lower the melting point of the polymer; formulations in which this occurs are used in thermoforming or blow molding. [694] Polypropylene can be isotactic, syndiotactic, or atactic, depending on the orientation of the pendant methyl groups attached to alternate carbon atoms. In isotactic polypropylene (Figure 1.2), the most common commercial form, pendant methyl groups are all in the same configuration and are on the same side of the polymer chain. Due to this regular, repeating arrangement, isotactic polypropylene has a high degree of crystallinity. In syndiotactic polypropylene, alternate pendant methyl groups are on opposite sides of the polymer backbone, with exactly opposite configurations relative to the polymer chain. Syndiotactic polypropylene is now being produced commercially using metallocene catalysts. In atactic polypropylene, pendant methyl groups have a random orientation with respect to the polymer backbone. Amounts of isotactic, atactic, and syndiotactic segments in a formulation are determined by the catalyst used and the polymerization conditions. Most polymers are predominantly isotactic, with small amounts of atactic polymer. New metallocene catalysts make possible other stereochemical configurations, such as hemi-isotactic polypropylene. In this configuration, most pendant methyl groups are on the

Chemistry

1.3.1 Stereochemistry Because of its structure, isotactic polypropylene has the highest crystallinity, resulting in good mechanical properties such as stiffness and tensile strength. Syndiotactic polypropylene is less stiff than isotactic but has better impact strength and clarity. Due to its irregular structure, the atactic form has low crystallinity, resulting in a sticky, amorphous material used mainly for adhesives and roofing tars. [794, 691] Increasing the amount of atactic polypropylene in a predominantly isotactic formulation increases the room temperature impact resistance and stretchability but decreases the stiffness, haze, and color quality. [695] The amount of atactic polypropylene in a polypropylene formulation is indicated by the level of room temperature xylene solubles; levels range from about 1–20%. [771] Polypropylenes generally have higher tensile, flexural, and compressive strength and higher moduli than polyethylenes due to the steric interaction of the pendant methyl groups, which result in a more rigid and stiff polymer chain than in polyethylene. [693] General effects of atactic level on the properties of polypropylene are listed in Table 1.1. [695, 642, 693] 1.3.2 Molecular weight and melt flow index Longer polypropylene chain lengths result in a higher molecular weight for the polymer. The weight-average molecular weight of polypropylene generally ranges from 220,000–700,000 g/mol, with melt flow indices from less than 0.3 g/10 min. to over 1000 g/10 min. The melt flow index (MFI) provides an estimate of the average molecular weight of the polymer, in an inverse relationship; high melt flow indicates a lower molecular weight. [693, 642, 696, 797] Viscous materials with low MFI values (3 plastic, that is to say it softens when heated and hardens when cooled. It is hard at normal ambient temperatures, and it is this that allows the thermoplastic property to be exploited in economical processing techniques such as injection molding or extrusion. The softening point, or resistance to deformation under heat, of a thermoplastic limits its service temperature range. The upper permissible limit may be defined as a maximum operating temperature, or as a heat distortion temperature at a given stress level. The operating range of polypropylene is markedly superior to those of the so-called commodity plastics, and is excelled — sometimes by a substantial margin — only by the far more costly

Figure 12.18 Wöhler (S-N) plot for Hoechst Hostacom M2 N01 20% talc filled polypropylene at 23°C and 10Hz.

Figure 12.17 Low frequency (0.5 Hz) fatigue per-

Figure 12.19 Wöhler (S-N) plot for Hoechst Hosta-

formance of polypropylene (semi-crystalline) compared to polycarbonate (amorphous). [1158]

com G3 N01 30% coupled glass fiber reinforced polypropylene at 23°C and 10Hz.

Design principles


121 “engineering plastics” (Table 12.7). If the product has a wide working temperature range, then the coefficient of linear expansion becomes significant and must be allowed for in assemblies. The coefficient for polypropylene is somewhat higher than most commodity plastics but is less than that of polyethylenes. The operating temperature range of polypropylenes is considerably affected by the use of reinforcements and modifiers (Table 12.8). The heat distortion temperature of talc filled grades is 25°C to 30°C higher than basic grades at the lower stress level, while coupled glass grades extend the figure to 160°C. The effect of talc fillers is far less dramatic for heat distortion temperatures measured at the higher stress level, but coupled glass grades again excel with a performance some 90°C better than basic grades. The heat distortion performance and maximum operating temperature of elastomer modified grades is substantially less than that of

Figure 12.20 Smith diagram for Hoechst Hostalen PPH 2250 polypropylene homopolymer at 23°C and 10 Hz, based on alternating tensile and compressive stress, and repeated tensile stress.

Table 12.7 Thermal properties of polypropylene compared with other thermoplastics. [1103]

Polymer

Maximum operating temperature (°C )

Heat distortion temperature at 0.45 MPa (°C )

at 1.80 MPa (°C )

Linear expansion (mm/°C × 10–5)

PES

180

260+

203

PBT

120

150

60

12

Polycarbonate

115

143

137

7

PET

115

115

80

8

Polypropylene homopolymer

100

105

65

10

Acetal

90

160

110

11

Polypropylene copolymer

90

100

60

10

Polyamide 6

80

200

80

10

Polyamide 6/6

80

200

100

8

PPO

80

137

129

6

Polyamide 6/10

70

157

66

14

Polyamide 11

70

150

55

9

Polyamide 12

70

150

55

11

ABS

70

98

89

8

SAN

55

96

84

7

HD polyethylene

55

75

46

12

PMMA

50

103

95

7

Polystyrene, general purpose

50

90

80

7

Polystyrene, high impact

50

85

75

7

PVC-U

50

70

67

6

LD polyethylene

50

50

35

20


5.5

Design principles

122 basic grades. Fillers and reinforcements substantially reduce the coefficient of linear expansion. The coefficient of linear expansion for a plastics material varies with temperature, unlike those of metals which are substantially independent of temperature (Figure 12.21). For filled and reinforced grades of polypropylene the coefficient also varies with flow direction and orientation. Polypropylene is a semi-crystalline material consisting of crystalline regions or spherulites contained in an amorphous matrix. These two components behave differently when heated. The amorphous regions soften at a temperature known as the glass transition temperature or Tg. This is not melting but rather a change of state from a brittle or glassy condition to a rubbery or ductile condition. Those plastics with a glass transition temperature in excess of room temperature will fail under stress in a strong brittle manner at room temperature. The glass transition temperature of polypropylene is far below room temperature, so this tells us that the

material will fail in a tough ductile manner at normal temperatures (Table 12.9). At a higher temperature than the glass transition temperature, the crystallites or spherulites begin to lose cohesion. This is known as the crystalline melting point or Tm. At this point, the conversion to the plastic state is substantially complete. A further

Figure 12.21 Variation of coefficient of linear expansion of polypropylene with temperature (measured in flow direction). Key: a = non-reinforced base grade polypropylene, b = Hostacom M2 N01 (20% talc), c = Hostacom M2 N02 (20% talc, improved impact), d = Hostacom M4 N01 (40% talc), e = Hostacom G2 N02 (20% coupled glass fiber), f = Hostacom G2 N01 (20% glass fiber), g = Hostacom G3 N01 (30% coupled glass fiber), h = Hostacom M1 U01 (10% talc, easy flow), i = Hostacom M4 U01 (40% talc, easy flow), k = pure aluminum. [1004]

Table 12.8 Thermal properties of polypropylenes with various fillers, reinforcements and modifiers. [1103] Heat distortion temperature

Maximum operating temperature (°C )

at 0.45 MPa (°C )

at 1.80 MPa (°C )

Linear expansion (m/m/°C × 10–5)

Homopolymer

100

105

65

10

Homopolymer, UV stabilized

100

110

57

10

Copolymer

90

100

60

10

Copolymer, UV stabilized

90

100

60

10

20% talc filled

100

130

78

7

40% talc filled

100

130

80

5

20% calcium carbonate filled

100

105

68

6


100

110

71

4

20% glass fiber reinforced

100

122

93

4

30% glass fiber coupled

100

160

150

4

Fire retardant

100

110

70

9

Elastomer modified

90

82

55

11

Elastomer modified, UV stabilized

90

82

55

11

Structural foam

95

72

46

16

Polypropylene type

Design principles


123 rise in temperature will reduce the viscosity of the plastics melt but will not change its state any further. For most plastics, the lower end of the recommended range of processing temperatures will be well above the crystalline melting point, generally by 30°C to 50°C or more. When the plastics melt is cooled, the crystallites reform but do so at a temperature lower than the crystalline melting point. This temperature is known as the crystallization temperature and it is very much dependent on the cooling rate as well as the presence of fillers, clarifiers and nucleating agents. The crystallization temperature of polypropylene is in the range 100°C to 130°C. When polypropylene is exposed to high temperatures within its maximum operating temperature, a gradual deterioration takes place. The effect is known as thermal aging. It is an oxidation process and so is related to weathering. All polypropylenes are stabilized against oxidation but special long-term stabilizers are used in grades that must withstand sustained high temperatures or hot detergent solutions. Copper, manganese, cobalt and carbon black additives reduce the resistance of polypropylene to heat aging.

One measure of thermal aging resistance uses the concept of an induction period. This is the time in days taken for a sample held at 150°C to degrade by a prescribed extent. The induction period for polypropylene homopolymer ranges from 20 to 50 days, depending on the grade formulation. The corresponding range for block copolymers is 50 to 150 days. Random copolymers cannot be characterized by this test because of their lower melting points. The resulting test data make it possible to estimate the service life of polypropylene at elevated temperatures (Figure 12.22). For example, a polypropylene with an induction period of 20 days would have a service life of about 6 years at 80°C, while one with an induction period of 10 days would have a life of about 1,000 days. The thermal conductivity of plastics varies with temperature. At service temperatures most are poor conductors of heat, a property that is often exploited in design applications. The thermal conductivity of polypropylene is among the lowest to be found in thermoplastics (Table 12.10). The thermal conductivity of polypropylene is substantially increased by the inclusion of fillers and reinforcements, particularly by talc (Table 12.11).

Table 12.9 Glass transition and crystalline melting

12.2.3 Chemical resistance Polypropylene has a high resistance to chemical attack as a consequence of its non-polar nature. The term non-polar refers to the bond between atoms. The atoms of each element have a specific electronegativity value. The greater the difference between the electronegativity values of the atoms in a bond, the greater will be the polarity of the bond. When this difference is small the material is

points of polypropylene compared with other thermoplastics.

Polymer Acetal Polyethylene Polypropylene Polyamide 12 Polyamide 6/10 Polyamide 11 Polyamide 6 PBT Polyamide 6/6 PET Polystyrene PMMA PPO ABS SAN PVC-U Polycarbonate PES

Glass transition temperature (°C )

Crystalline melting temperature (°C )

–50 –33 –10 37 40 46 50 50 50 69 100 90–105 104–120 80–125 115–125 87–135 150 230

181 110–140 165–176 179 227 194 220 240 265 267 240 160 190 212 220 -


Figure 12.22 Service life of polypropylene. [1016]

Design principles

124 Table 12.10 Thermal conductivity of polypropylene

Table 12.11 Effect of fillers on thermal conductivity of

compared with other thermoplastics.

polypropylenes. [1004]

Polymer

Thermal conductivity at 20°C (W/m.K)

PVC-U

0.14–0.17

Polypropylene type Polypropylene, unmodified

Thermal conductivity at 20°C (W/m.K) 0.17–0.22

ABS

0.18

20% talc filled

0.41

PES

0.18

40% talc filled

0.56

PMMA

0.18

0.40


0.18


SAN

0.18


0.25

PBT

0.21


0.30

Polycarbonate

0.21

Polypropylene

0.17–0.22

Polyamide 11

0.23

Polyamide 12

0.23

Polyamide 6/6

0.23

PPO

0.23

PET

0.24

Polyamide 6

0.29

Acetal

0.25–0.30

LD polyethylene

0.32–0.40

HD polyethylene

0.38–0.51

said to be non-polar. In other words, the solubility of a polymer is related to the forces holding the molecule together, and one measure of this is the solubility parameter δ which is the square root of the cohesive energy density (Table 12.12). Compatibility, that is to say vulnerability, occurs when the solubility parameters of the polymer and solvent are similar. As a very rough guide, the lower the value of the solubility parameter, the more resistant will be the polymer. On this basis, polypropylene rates better than any other melt-processable thermoplastic except polyethylene. Chemical resistance involves resistance to two principal mechanisms; solution and reaction. Solution is not accompanied by chemical change, and it occurs when a chemical dissolves the polymer. In many cases of solution, polymers are not dissolved outright but simply soften and may also swell. These effects are often reversible when the solvent chemical is driven off. Reaction on the other hand, does involve chemical change and is usually irreversible. All types of chemical attack are more severe at higher temperatures and at higher concentrations of the chemical reagent.

Design principles

In broad terms, polypropylene is resistant to alcohols, organic acids, esters, and ketones. It is swollen by aliphatic and aromatic hydrocarbons, and by halogenated hydrocarbons. It is highly resistant to most inorganic acids and alkalis but is attacked by strong oxidizing acids and halogens. Contact with copper and copper alloys accelerates oxidation, particularly in the presence of fillers and reinforcements. Table 12.13 gives a rough design selection guide for chemical resistance. No table can account for possible synergy effects when exposure to a mixture of chemicals is expected: there is no substitute for testing in this case. 12.2.4 Electrical properties Most plastics are good electrical insulators but the properties of polypropylene rank near the best in each of the main measures of electrical performance (Table 12.14). These excellent electrical characteristics are an undoubted advantage, but an Table 12.12 Solubility parameters of some common plastics. [1101]

Polymer

Solubility parameter δ (MPa½)

PTFE

12.6

PCTFE

14.7

Polyethylene

16.3

Polypropylene

16.3

PMMA

18.7

Polystyrene

18.7

PVC

19.4

PET

21.8

Acetal

22.6

Polyamide 6/6

27.8


125 unwanted side effect is the propensity to build up static electrical charges on the surface. The static charges attract dust and soiling and create a spark potential which although harmless in normal circumstances is a danger in hazardous environments. The development of static charges can be alleviated by the use of anti-static agents. The electrical properties of polypropylenes are not greatly affected by common fillers, reinforcements, and modifiers (Table 12.15). For the most part, these additives are maintained as discrete bodies within and insulated by the polypropylene matrix, so it is the properties of the latter that prevail. An exception occurs if additives or foreign matter is present at the surface of the polypropylene. In such cases, the surface resistivity will be reduced. The electrical properties of polypropylene are unaffected by immersion in water and are relatively insensitive to temperature and frequency (Figure 12.23). There are two occasions when it is desirable to

Figure 12.23 The dissipation factor of polypropylene is relatively unaffected by temperature and frequency. [1106]

reduce the dielectric performance of polypropylene and this can be done by the inclusion of special additives. Electrostatic dissipative (ESD) grades are used in circumstances where normal anti-static grades are inadequate or are otherwise unsuitable, for example by virtue of the migratory mechanism. ESD grades would be needed for use in hazardous

Table 12.13 Chemical resistance basic guide for polypropylene. [1148] 70°F 120°F 70°F 120°F REAGENT (21°C) (49°C) REAGENT (21°C) (49°C) Acetic Acid (Glacial) S S Isooctane S S Acetic Acid (5%) S S Kerosene S NR Acetone S S Methyl Alcohol S S Ammonium Hydroxide (concentrated) S NR Mineral Oil, White NR NR Ammonium Hydroxide (10%) S S Nitric Acid (Concentrated) NR NR Aniline S S Nitric Acid (40%) NR NR Benzene S NR Nitric Acid (10%) S S Carbon Tetrachloride NR NR Oleic Acid S S Chromic Acid (40%) S NR Olive Oil S S Citric Acid (1%) S S Phenol Solution (5%) S S Cottonseed Oil S S Soap Solution (1%) S S Detergent Solution S S Sodium Carbonate Solution (20%) S S Diethyl Ether S NR Sodium Carbonate Solution (2%) S S Dimethyl Formamide S S Sodium Chloride Solution (10%) S S Distilled Water S S Sodium Hydroxide Solution (60%) S S Ethyl Acetate S NR Sodium Hydroxide Solution (10%) S S Ethyl Alcohol (95%) S S Sodium Hydroxide Solution (1%) S S Ethyl Alcohol (50%) S S Sodium Hypochlorite Solution (4 to 6%) S NR Ethylene Dichloride S NR Sulfuric Acid (Concentrated) NR NR Heptane NR NR Sulfuric Acid (30%) S S Hydrochloric Acid (Concentrated) S S Sulfuric Acid (3%) S S Hydrochloric Acid (10%) S S Toluene NR NR Hydrofluoric Acid (40%) S S Transformer Oil S M Hydrogen Peroxide Solution (28%) S S Turpentine S S Key: S = Satisfactory M = Marginal NR = Not Recommended Hydrogen Peroxide Solution (3%) S S


Design principles

126 environments or in contact with semi-conductor devices. Carbon black is typically used as a conductive filler in ESD grades of polypropylene. The other reason to increase the conductivity of polypropylene is to provide shielding against electromagnetic interference (EMI) and/or radio frequency interference (RFI). Many electronic and electrical devices such as computers emit signals which may interfere with communications, so regulations now require that these devices be shielded to eliminate or attenuate these signals. The plastics enclosures normally used to house such devices provide no shielding, so secondary measures are needed either in the form of conductive paints on the inner surface, or as a thin sheet metal lining held within the housing. If the plastics housing can be made sufficiently conductive, it will act as a shield so eliminating the cost of secondary measures. Carbon black is not sufficiently conductive, so EMI shielding grades of polypropylene use a range of additives including metal

powders, flakes and fibers, and even composite additives such as nickel-coated graphite fibers. 12.2.5 Environmental stress cracking One of the major advantages of polypropylene is its apparently complete resistance to attack by environmental stress cracking. The phenomenon is a leading cause of service failure in plastics parts, accounting for perhaps 15% of all observed cases. Environmental stress cracking, often referred to as ESC, causes a stressed plastics part to become brittle and crack when in contact with a wide range of fluids that act as stress cracking agents. It is the combination of stress and fluid contact that causes failure to occur much earlier than either component could achieve in isolation, if at all. It is not easy, other than by experiment, to identify potential stress cracking agents for any plastics material. Solvents will frequently act as stress cracking agents, but some fluids including surfactants that have very little effect in isolation on a particular

Table 12.14 Electrical properties of polypropylene compared with other thermoplastics. [1103] Volume resistivity (log ohm cm)

Dielectric strength (MV/m)

Dielectric constant (1kHz)

Dissipation factor (1kHz)

PES

17.5

16

3.5

0.0021


17

28

2.3

0.0005


17

28

2.28

0.0001

Polycarbonate

17

23

3

0.001

HD polyethylene

17

22

2.3

0.0005

PPO

17

21

2.6

0.0004

LD polyethylene

16

27

2.3

0.0003

SAN

16

25

3

0.01


16

20

2.6

0.0002

ABS

16

20

2.8

0.007


16

15

2.8

0.0006

Polyamide 12

15

60

3.6

0.05

PMMA

15

25

3.3

0.03

Polyamide 6/6

15

25

8

0.2

Acetal

15

20

3.7

0.0015

PBT

15

20

3.2

0.002

PET

15

17

3.3

0.002

Polyamide 6

14

25

8

0.2

Polyamide 11

14

20

4

0.05

PVC-U

14

14

3.1

0.025

Polyamide 6/10

13

20

4.7

0.09

Polymer

Design principles


127 Table 12.15 Electrical properties of polypropylenes with various fillers, reinforcements and modifiers. [1103] Volume resistivity (log ohm cm)

Dielectric strength (MV/m)

Dielectric constant (1kHz)

Dissipation factor (1kHz)

Homopolymer

17

28

2.28

0.0001


16

28

2.3

0.0001

Copolymer

17

28

2.3

0.0005


17

28

2.3

0.0005

20% talc filled

16

20

2.5

0.002

40% talc filled

16

20

2.6

0.006


15

18

2.6

0.002


15

18

2.8

0.002


16

22

2.6

0.001


16

20

2.7

0.001

Fire retardant

14

23

2.5

0.002

Elastomer modified

15

28

2.3

0.0005


15

28

2.3

0.0005

Structural foam

16

26

2.2

0.001

Polypropylene type

plastics material, are known to be potent stress cracking agents. It is important to remember that a plastics component need not be externally loaded or stressed to suffer from environmental stress cracking. Manufacturing processes, particularly injection molding, result in residual stresses frozen into the component, and these can be quite sufficient to initiate failure by environmental stress cracking. Neither is it necessary for a plastics part to be immersed in a stress cracking agent to be at risk. Apparently mundane and benign treatments with a range of agents including paints, inks and lacquers, adhesives, plasticizers and lubricants, and rust-proofing fluids are known to result in environmental stress cracking. Polyethylene, a chemically close relative of polypropylene, does suffer to an extent from environmental stress cracking but polypropylene itself appears to be entirely free of the problem. Failures are known when polypropylene is exposed to strong oxidizing agents such as bleaches. These are sometimes wrongly described as environmental stress cracking but in fact are examples of chemical attack that may be enhanced by stress. The proper term for this phenomenon is corrosion stress cracking or CSC. 12.2.6 Water absorption The water absorption of polypropylene is very low and is less than that of most other plastics with the


exception of low density polyethylene (Table 12.16). This characteristic is due to the non-polar nature of the material. Polypropylene is water repellent, does not swell in water, and is unaffected in properties and dimensions by changes in relative humidity. In warm humid atmospheres there can be a very small uptake of water, but the effect is entirely due to surface adsorption. The low water absorption of polypropylene is largely unaffected by fillers, additives, and reinforcements, although a marginal increase does occur with the use of calcium carbonate fillers (Table 12.17). 12.2.7 Permeability Permeability is a property that assumes importance when a plastics material is provided in relatively thin sections, particularly as films but also as thinwall injection and blow moldings. It is a measure of the resistance of the material to the transmission of gases and vapors and is of the utmost importance in packaging applications. It implies that the plastics film or barrier separates two distinct and different regimes. Typically, it separates the contents of a package from the normal atmospheric environment. Degradation of the pack contents or the environment may occur if agents can permeate through the barrier in either direction. Transmission begins when an agent or penetrant dissolves into an exposed barrier surface. This cre-

Design principles

128 Table 12.16 Water absorption of polypropylene

Table 12.17 Water absorption of polypropylenes with

compared with other thermoplastics. [1103]

various fillers, reinforcements and modifiers. [1103]

Polymer

Water absorption (%)

Polypropylene type

Water absorption (%)

LD polyethylene

0.01

Homopolymer

0.02


0.02


0.02

HD polyethylene

0.02

Copolymer

0.03


0.03


0.03


0.05

20% talc filled

0.02

PPO

0.07

40% talc filled

0.02

PVC-U

0.1


0.04

PET

0.1


0.04

PBT

0.1


0.03

Polycarbonate

0.15


0.02


0.2

Fire retardant

0.01

Acetal

0.22

Elastomer modified

0.02

SAN

0.25

0.02

Polyamide 12

0.25


Polyamide 11

0.3

Structural foam

0.02

PMMA

0.3

ABS

0.3

Polyamide 6/10

0.4

PES

0.43

Polyamide 6/6

1.2

Polyamide 6

1.5

ates a concentration gradient within the barrier and results in diffusion of the penetrant across the thickness of the barrier. The transmission mechanism is completed by evaporation of the penetrant from the second surface of the barrier. Evaporation tends to maintain the concentration gradient and so perpetuates the transmission mechanism. The transmission rate is inversely proportional to the barrier thickness and increases as the temperature rises (Figure 12.24). The two key aspects of permeability are water vapor transmission and gas permeability. Polypropylene is highly impermeable to water vapor and is bettered in its performance only by specialized packaging materials such as PVDC (polyvinylidene chloride) and CTFE (chlorotrifluoroethylene). Biaxially oriented polypropylene performs significantly better than cast film because the orientation of the molecules reduces the intermolecular space available for the diffusion mechanism (Table 12.18).

Design principles

Polypropylene performs less well on gas vapor transmission, although once again it is improved markedly by orientation. Nevertheless, a number of materials are clearly superior, for example as oxygen barriers (Table 12.19). No thermoplastic emerges as an ideal low permeability film material. A few have excellent resistance to water vapor and gases but are expensive or mechanically weak. Others such as polypropylene have very good resistance to water vapor transmission but are less effective against gases. Still other materials show the converse behavior. For this reason it has become very common to use coextrusion and laminating processes to produce multilayer packaging films in order to combine the advantages of several materials. These multilayer constructions may consist solely of a number of different plastics, or they may include other materials such as paper or metal foil. Polypropylene is commonly used for the outer layers of multilayer films where it confers strength, economy and protection to inner specialized barrier layers. Biaxially oriented polypropylene (BOPP) is particularly important in packaging, and is the predominant film for biscuit and snack foods applications. The performance is often improved with barrier resin coatings, particularly using PVDC. Consumption of BOPP is growing at some 10% per annum. Typical applications include:


129

cigarette packing shirt packaging flower wraps shrink wraps biscuit and snack food packages

12.2.8 Food and water contact Polypropylene itself is intrinsically safe. The base material is generally accepted to be non-toxic and non-carcinogenic. Acute and chronic animal feed trials have revealed no damage attributable to polypropylene, neither has there been any evidence of the material acting as an irritant for skin or mucous membranes. Any worry about using polypropylene for contact with foodstuffs or potable water arises from the use of additives in the material, particularly where there is a possibility of these migrating or leaching. All manufacturers of polypropylene produce grades that are safe to use in food or potable water contact applications. Safety in this context is judged according to regulations that vary from country to country. The leading authorities are the Food and Drug Administration (FDA) for the USA, and the appropriate European Directives for the countries of the European Union. Somewhat different regulations, although with the same general thrust, may be applied by the various national water authorities. Provided that approved grades are used and that compliance is checked with the appropriate national regulations, there will be no difficulty in using polypropylene in contact with foodstuffs or potable water. On the contrary, the material has an important role, in the packaging of foods in particular. 12.2.9 Sterilization Polypropylene itself has no nutritional value for microorganisms and so is not attacked by them. The material cannot be penetrated by microorganisms unless porosity is present. This is unlikely in polypropylene films thicker than 0.1 mm so


Table 12.18 Water vapor transmission of polypropylene compared with other thermoplastics. [1158]

Polymer

Water vapor transmission at 90% relative humidity (gm/mm/m2/day)

CTFE

0.005

PVDC

0.1

Polypropylene (oriented)

0.1

HD polyethylene

0.2

Polypropylene

0.3

LLDPE

0.4

LD polyethylene

0.5

EVOH

0.5–2

PET

0.6

Ethylene ionomer

0.6

PVC-U

1

Polystyrene

3

Polycarbonate

3

Polyamide 6

3

PBT

3

EVA

3

ABS

3

PVC-P

5

Polyamide 6/6

5

Figure 12.24 Temperature dependence of polypropylene to gas permeability and water vapor transmission rate. [1064]

Design principles

130 the material forms an effective barrier against microorganisms. This property, together with cheapness, versatility, and a fundamentally non-toxic nature makes the material an important contender for medical applications (syringes, packaging) as well as for food use. Both application areas raise the question of resistance to sterilization procedures. A number of different techniques are in common use: irradiation by gamma rays, beta rays, or by electron beam gas treatment by ethylene oxide, ethylene chlorohydrin, or ethylene glycol heat treatment by steam autoclave or dry oven bactericidal treatment by disinfectants and cleaning agents Of these treatments, gamma radiation is now probably the most important for polypropylene. Gamma rays are more penetrative than electron beam or beta rays, so the method is effective with relatively thick-walled moldings or pre-packaged articles. The high energy treatment is capable of breaking chemical bonds, and in the case of polypropylene, both yellowing and embrittlement effects

are likely to be encountered. To counteract this tendency, the manufacturers of polypropylene have developed specially stabilized grades for medical applications. These radiation stabilizers are an active area of research and solutions are mostly regarded as proprietary. The function of the stabilizer packages is crucial. These special grades of polypropylene are highly successful in medical markets although normal grades would fail through excessive irradiation embrittlement. The effect of irradiation depends mainly on the dose and the irradiation time. Sterilization is usually performed with a gamma radiation dose of 2.5 Mrad or more. Random and block polypropylene copolymers tend to be less prone to embrittlement than homopolymers. The once dominant ethylene oxide gas sterilization treatment is now in decline. The material has been declared mutagenic by the US Environmental Protection Agency and special precautions are necessary in its use. Environmental pressure has also focused on the use of CFCs as a carrier gas for the ethylene oxide although this has now been dealt

Table 12.19 Gas vapor transmission of polypropylene compared with other thermoplastics. [1158]

Polymer

Oxygen transmission rate (cm3/mm/m2/atm/day)

Nitrogen transmission rate (cm3/mm/m2/atm/day)

EVOH

> 0.01

PVDC

0.05

0.1

2

Polyamide 6

0.6

0.35

3

Polyamide 6/6

0.6

0.3

3

PET

2

0.3

6

CTFE

3

0.5

14

PVC-U

7

7

15

PBT

15

3

140

ABS

50

-

150

Polypropylene (oriented)

60

17

200

HD polyethylene

75

20

200

Polypropylene

90

22

250

Polycarbonate

100

13

500

Polystyrene

120

20

400

PVC-P

140

70

900

Ethylene ionomer

150

-

-

LD polyethylene

200

60

700

LLDPE

200

-

-

EVA

300

-

1100

Design principles

> 0.0015

Carbon dioxide transmission rate (cm3/mm/m2/atm/day) > 0.01


131 with by the substitution of carbon dioxide or chlorotetrafluoroethane as carriers. A further difficulty is the need to maintain residual gas levels in the sterilized product below guidelines set by the regulatory authorities like the US Food and Drug Administration. Nevertheless, the ethylene oxide gas treatment remains a significant sterilization technique. Polypropylene is generally regarded as substantially unaffected by the treatment. Steam autoclaving is generally carried out at temperatures of 120°C to 135°C. Polypropylenes are resistant to high temperatures and highly resistant to water, so they are entirely unaffected by autoclaving provided the treatment temperature is kept below the polypropylene softening range. For homopolymers and block copolymers the guideline softening range is 155°C to 165°C. For random copolymers the range is rather lower at 135°C to 150°C.

temperatures, will help to do this. However, low mold temperatures will tend to reduce surface gloss. Polypropylene displays the phenomenon of contact transparency whereby the transparency of a container appears to be improved by contact with the enclosed liquid. The property means that standard polypropylenes are usually good enough for containers where it is necessary to see the liquid level. The transparency of polypropylenes can be considerably improved by the use of additives that act upon the growth and size of the crystal structure (Table 12.20). These additives are known as nucleators and clarifiers. 12.2.11 Fire behavior Polypropylene is a combustible material (Table 12.21). It ignites spontaneously at about 360°C and can be ignited from an external source at about 345°C. If the ignition source is removed, the material will continue to burn with a pale luminous flame. The burning material melts and produces burning droplets which have the potential to spread the fire. Burning polypropylene will stick to the skin and cause severe burns. Fillers, reinforcements, and modifiers have little effect on the fundamental flammability of polypropylene (Table 12.22) but they may have a bearing on the tendency to drip and will also contribute to the products of combustion. However, the flammability of polypropylene can be improved considerably by the use of flame retardant additives. When polypropylene is pyrolized at low concentrations of oxygen, a range of relatively simple hydrocarbons is formed at low and intermediate temperatures. At high temperatures, polycyclic aromatic hydrocarbons are produced. In fires with a relatively low oxygen level, oxygenated organic species are produced, including acrolein which is a severe irritant. The products are less in evidence at higher temperatures and oxygen levels (Table 12.23).

12.2.10 Transparency and optical properties The transparency of a material depends on surface smoothness as well fundamental structure. It is defined in terms of two measures — transmittance and haze. A material with good transparency will have high transmittance and low haze. Transmittance is the ratio of transmitted light to incident light. Reflectance — the ratio of reflected light to incident light — is the complementary measure. For an ideal material, the sum of transmittance and reflectance would be unity. For real materials, the difference between unity and the sum of transmittance and reflectance represents light absorbed. Haze is the ratio of incident light passing through the specimen which deviates within a given angle by forward scattering. The principal factor that mediates the transparency of polypropylene is its semi-crystalline structure. Light is scattered at every boundary between the crystalline and amorphous phases, and so the transparency is directly dependent on the size and concentration of crystalline spherulites in the polypropylene. Random copolymers are Table 12.20 Optical properties of polypropylene random copolymer. [1016] more transparent than block coTransparency Haze polymers or homopolymer. ASTM D 1746 ASTM D 1003 The transparency of polyproComponent % of value for air % of value for air pylene articles can be improved by Flask with 0.5mm wall thickness 2.0 17 using molds or dies that impart a Injection molded disc 2mm thick high surface gloss and by using - without nucleating agent 0.3 86 process conditions that reduce the - with nucleating agent 18 35 size of spherulites. Rapid cooling, The refractive index of polypropylene is 1.49. coupled with low melt and mold


Design principles

132 12.2.12 Weathering and light stability The weathering performance of a material refers to its ability to withstand the natural environment; light stability is only one aspect of this, although a very important one. Weathering is an imperfect term in that it embraces many separate and highly variable effects. Weather testing too is an imprecise science while accelerated weather testing procedures correlate imperfectly with long-term exposure tests. The key factors at work in the weathering process — and these vary widely from one geographical location to another — are: solar radiation moisture in the form of humidity, condensation or rain temperature pollutants including ozone, acid rain, and soiling Table 12.21 Fire behavior of polypropylene compared with other thermoplastics. [1103]

microbiological attack salt water Depending on the material exposed, many or even most of these factors may be at work simultaneously and perhaps synergistically. The first signs of weathering damage always appear as surface changes or defects but with continued exposure the changes can extend into the body of the material, for example by crack propagation from the surface. Weathering damage then, may entail anything from a slight color change to complete fracture failure. In the case of polypropylene, microbiological attack is not a problem, neither is the material susceptible to damage by moisture acting in isolation. The principal problem is solar radiation and more specifically, ultraviolet radiation. Some 6% of solar radiation consists of wavelengths below 400nm. This is the ultraviolet region. The midrange UV-B radiation with a wavelength in the range 290 nm to 315 nm is by far the most damaging. The intensity of UV-B radiation is related to the angle of solar altitude and is at its most severe in regions with high solar altitudes, namely in the tropics. UV-B radiation is completely absorbed by

Polymer

Flammability (UL94)

Oxygen index (%)

PVC-U

V0

45

PES

V0

36

Polycarbonate

V2

25

Polyamide 11

V2

22

Polyamide 12

V2

21

Polypropylene type

PBT

HB

25

Polyamide 6/10

HB

23

Polyamide 6

HB

Polyamide 6/6

Table 12.22 Fire behavior of polypropylenes. [1103] Flammability (UL94)

Oxygen index (%)

Homopolymer

HB

17

HB

17

22


HB

22

Copolymer

HB

17

PET

HB

20


HB

17

PPO

HB

20

20% talc filled

HB

17

ABS

HB

19

40% talc filled

HB

18

PMMA

HB

19

17

HB

18


HB


18

HB

18


HB


17

HB

18


HB

SAN Polypropylene copolymer

HB

17


HB

17


HB

17

Fire retardant

V0

28

Elastomer modified

HB

17

HD polyethylene

HB

17

17

HB

17


HB

LD polyethylene Acetal

HB

15

Structural foam

HB

17

Design principles


133 Table 12.23 Compounds produced b y polyprop ylene at three stages of fire in lo w ventilation. [1158] Fire growth stage (ppm)

Fire steady state (ppm)

Fire decay stage (ppm)

Fire growth stage (ppm)

Fire steady state (ppm)

Fire decay stage (ppm)

Methane

0.2

◊

◊

Hexene

0.3

0.4

0.1

Acetylene

2.8

0.6

1.2

Benzene

72.1

809.9

575.1

Ethylene

2.4

2020.9

899.4

Cyclohexadiene

0.5

0.1

Ethane

5.1

977.5

349.4

Heptene

1.2

◊

Propene

3.3

31.2

3.7

Toluene

54.5

56.5

31.6

Propyne

◊

25.7

6.2

Octene

1.6

0.4

0.6

Methanol

0.5

6.2

12.7

Octadiene

◊

0.2

0.1

Acetaldehyde

2.7

3.9

2.5

Xylene

43.0

26.5

15.1

Butene

0.5

18.3

3.1

Styrene

32.2

5.6

12.5

10.7

12.3

26.4

2.8

Compound

Compound

◊

Butadiene

◊

◊

Nonene

Cyclobutane

◊

◊

Benzaldehyde

0.7

0.1

Indene

0.4

1.7

Ethyl styrene

◊

7.1

1.9

Decene

◊

◊

◊

Methyle indene

◊

19.6

2.7

6.0

204.8

103.0

◊

Butane Ethanol

3.1

Acrolein

◊

◊

7.0

Acetone

899.2

216.2

32.5

23.9

1.1

Naphthalene

◊

◊

Methyle naphthalene

5.4

7.3

Key: ◊ = present in a concentration too low to measure

Cyclopentadiene ◊

Pentadiene Crotonaldehyde

17.2

the ozone layer at solar altitudes of less than 14°. It is also absorbed by window glass. UV-C radiation (100 nm to 290 nm) is fully absorbed in the ozone layer at all solar altitudes. Like other polyolefins, polypropylene is highly susceptible to damage by exposure to the UV radiation in sunlight. The surface deteriorates by crazing to a chalky friable material of very low strength. The effect leads to the complete failure of films but in the case of moldings, the damaged surface can be scratched away to reveal a substantially unchanged substrate. Small molded features such as snap-fits and lugs are likely to fracture completely. The mechanism of UV polypropylene failure is akin to oxidation and since crystalline regions are more impervious to oxygen than amorphous regions, the more crystalline nucleated polypropylenes have a somewhat better resistance to UV degradation than less crystalline types. For the same reason, degradation proceeds more slowly in oriented polypropylenes. Although those pigments that are opaque to UV radiation can give a measure of protection, the fact remains that polypropylene is intrinsically un-

© Plastics Design Libr ary

◊

suited to sunlight exposure unless it is specially stabilized to resist photo-oxidation (Figure 12.25). Even then, there is likely to be some minor deterioration of the surface. The effect can often be noticed on garden furniture and stadium seating. These specially stabilized grades are modified by means of UV stabilizer additives.

Figure 12.25 Effect of UV stabilizers on polypropylene block copolymer. [1016]

Design pr inciples

134 12.2.13 Surface properties 12.2.13.1 Hardness The surface hardness of polypropylene is less than that of other thermoplastics with the exception of polyethylene (Table 12.24). However, it is sufficient to resist scratching with a fingernail. Hardness decreases as the temperature rises and increases with greater crystallinity. The surface hardness of polypropylene is essentially independent of fillers and reinforcements, although elastomeric modifiers are likely to reduce the figure. 12.2.13.2 Sliding Polypropylene is rarely used as a sliding or bearing material except in isolated applications such as conveyor belt guide bars for the beverage industry. The friction performance of a few special grades has been improved by means of silicone and/or PTFE additives. A low coefficient of friction is obviously desirable in a bearing. The coefficient is difficult to determine and depends very much on test conditions. Two cases are important: the plastics material bearing against itself, and the plastics material bearing against a foreign material. In the latter case, polished steel is generally used as a reference Table 12.24 Hardness of polypropylene compared

standard. For each case there are two instances. The coefficient of friction observed when moving a body from rest is the static coefficient of friction. The figure observed in a body under steady motion is the dynamic or kinetic coefficient of friction. It is desirable in a bearing material for there to be little difference between the static and dynamic coefficients. The published figures for static and dynamic coefficients must be compared with caution. Dynamic coefficients are often measured at a higher load than static coefficients, and this makes any direct comparison between the figures difficult or impossible. To make matters worse, published figures often omit the test conditions. Consequently, and although it is ostensibly an easy matter, in practice it is difficult to establish from reported figures whether the static coefficient is greater or less than the dynamic coefficient. Instances of both cases have been reported. A material whose static coefficient was the greater would exhibit a “stick-slip” behavior. If the dynamic coefficient was the greater, the behavior would be the less familiar “slip-stick”. For practical purposes, the dynamic coefficient is generally the more appropriate measure (Table 12.25). Table 12.25 Dynamic coefficient of friction for polypropylene compared with other basic grades of thermoplastics. [1218]

with other thermoplastics.

Polymer PET PMMA PBT

Ball indentation hardness (N/mm2) 200 180–200

Polymer PBT Polypropylene

Polymer on polymer (Dynamic coefficient)

Polymer on steel (Dynamic coefficient)

0.24

0.13

-

0.23

180

PVC

0.17

0.25

Acetal

150–170

PET

-

0.25

SAN

130–140

HD polyethylene

-

0.26


120–130

Polyamide 6

-

0.26

Polycarbonate

110

Polyamide 12

-

0.27

Polyamide 6/6

100

Polyamide 6/6

0.07–0.12

0.28–0.45

ABS

80–120

Polyamide 6/10

-

0.31

PVC-U

75–155

Polystyrene

-

0.32

Polyamide 6

75

PES

-

0.32

Polyamide 11

75

SAN

-

0.33

Polyamide 12

75

ABS

-

0.35

HD polyethylene

40–65

Acetal

0.4

0.35

Polypropylene

36–70

Polycarbonate

0.37

0.38

LD polyethylene

13–20

PMMA

-

0.4

Design principles


135 The performance of a bearing also depends on two other factors, the PV limit and the K-factor. The PV limit describes a limiting value of the product of bearing pressure and sliding velocity. Above this limit the bearing surface fails in some way, generally in the case of a plastics bearing by generating excessive temperatures. Bearing wear is proportional to the product of bearing pressure and sliding velocity. The constant that describes this proportionality is known as the K-factor or wear factor. A good bearing material should have a high PV limit and a low K-factor. Because polypropylene is not used significantly in sliding and bearing applications, quantitative data for the friction, PV limit, and K-factor values is very scanty. 12.2.13.3 Wear Wear occurs when a plastics material slides or rubs against another body or counterface. There are two main mechanisms for wear. When a plastics materials slides against a smooth counterface, the principal mechanism is adhesive wear. In this case, trace fragments of the plastics surface bond under frictional heat and pressure to the counterface. When the counterface is rough, abrasive wear occurs. In abrasive wear, trace fragments of the plastics surface are eroded by prominences on the countersurface. This produces debris that may augment the erosion process. Wear is difficult to measure (Table 12.26) and predict, being influenced by a wide range of factors, including: temperature bearing load sliding speed sliding distance motion — continuous, reciprocating, vibrating material of the counterface surface roughness of the counterface heat transfer environmental cleanliness external lubrication

12.3 Other factors influencing design 12.3.1 Orientation Orientation is a product of flow and a consequence of long-chain molecules. Orientation effects arise from the fact that the forces of attraction between units in the molecular chain greatly exceed the forces of attraction between adjacent chains. The significance of this is that strength can be maximized by orienting the molecules in a common direction. Concomitant disadvantages are that orientation minimizes strength in the transverse direction and results in anisotropic shrinkage during cooling leading to distortion. Where transverse strength is important, the molecules may be oriented in two orthogonal directions. This is known as biaxial orientation. Molecular orientation can be brought about by melt flow, for example during injection molding or extrusion, or by cold flow during stretching processes performed on monofilament or film. A third type of orientation, that of reinforcing fibers, is also significant. The term orientation is applied indiscriminately to all three phenomena and this can lead to some confusion. Polypropylene is a semi-crystalline material in the solid state. The regularity of the polymer chain structure allows neighboring chains to form regular or crystalline regions within an amorphous matrix. There is orientation of the polymer chains within a crystalline region, but orientation of one crystalline region with another may be quite random. In the melt state, polypropylene becomes fully amorphous. If it is then formed in a relatively stress-free manner, for example by casting and cooled, the crystalline regions will reform in random orientation. However, because polypropylene and indeed all thermoplastics have high melt viscosities, most melt processes involve high or very high shear stresses and shear rates. The shear rates are generated by polymer flow (Figure 12.26) and have the effect of

Table 12.26 Abrasion resistance of polypropylene compared with other thermoplastics. [1016]

Polymer

Weight loss by abrasion under 1kg load (mg/1000 cycles)

Polyamide

4–7

PVC

12

Polypropylene HD polyethylene


18–28 25

Figure 12.26 Flow of thermoplastics material in a channel.

Design principles

136

Figure 12.27 Variation of shear rate and orientation across the flow channel. [1175]

orienting the long polymer chains in substantially parallel formations. The degree of orientation is proportional to shear rate, and the extent to which it survives cooling and solidification depends on the rate of cooling. If cooling is very slow, a substantial degree of chain relaxation and disorder is reintroduced. However, if cooling is rapid, as it tends to be in industrial processes, then the orientation is largely retained or “frozen in”. One instinctively visualizes melt flow orientation as a lining-up of the molecular chains in the direction of flow but this is only partially true. The shear rate varies across the thickness of a flow channel, and therefore so too does orientation. When a thermoplastic flows through a relatively cold mold channel, a thin frozen layer quickly forms against the mold and the remaining flow takes place within this plastics “skin” (Figure 12.27). There is zero shear within the skin layer and little or no orientation. The shear rate varies across the remainder of the flow channel and is at a maximum near the frozen skin. Here there is a high degree of orientation. Shear rates in the center of the flow channel are much lower and so the degree of orientation is much less and may even approach the random state. The orientation of reinforcing fibers as a result of melt processing follows a similar but not identical pattern. Here the disparity between popular visualization and what really happens can lead to surprising results and design errors. Fiber orientation in and near the frozen skin follows the molecular pattern but in the center of the flow channel where shear rates are low, the fibers instead of being lightly or randomly oriented are actually strongly oriented transverse to the flow direction. As a generalization, melt flow orientation is an unplanned and largely unwanted side effect of polymer flow. In injection molding it is usually a disadvantage. Extrusion on the other hand, is a steady-state process involving constant geometry, so it is easier to foresee orientation effects and turn them to advantage.

By contrast, cold flow orientation is a premeditated action aimed at improving the strength of the material. This is performed by stretching monofilament, tape or film at controlled rates at a temperature below the crystalline melting point of polypropylene, and results in a partial orientation of molecular chains in the direction of stretch. Tensile strength is greatly increased in the direction of stretch while elongation at break is much reduced. Monofilaments and tapes are stretched in a single axial direction; the process is known as monoaxial or uniaxial orientation. Films need strength in all directions and this is usually achieved by stretching in two orthogonal axes. The process is known as biaxial orientation and is of great importance in the production of polypropylene film which is often known as BOPP (biaxially oriented polypropylene) film. 12.3.2 Distinction between homopolymer, random copolymer, block copolymer Commercial grades of polypropylene are available in three distinct forms — homopolymer, random copolymer, and block copolymer. Homopolymer is produced by polymerizing only propylene monomer. The result is a long chain molecule composed only of propylene groups or units. Copolymer is produced by polymerizing propylene together with minor proportions of secondary monomers, generally ethylene or butene. The result again is a long chain molecule but this time with ethylene or butene units interposed between propylene units. The process can be controlled by polymerization chemistry so that the secondary units are present either as relatively long sequences (block copolymers) or as short sequences or individual units (random coCompound 12%

Block copolymer 21%

Homopolymer 62% Random copolymer 5%

Figure 12.28 Consumption of polypropylene types in Western Europe, 1995. [1219]

Design principles


137 polymer). Recent figures for Europe suggest that homopolymer accounts for some 60% of polypropylene consumption while random copolymer occupies a relatively minor though growing market share of about 5% (Figure 12.28). The three forms overlap to an extent but do have some broad characteristics that help to dictate the optimum material choice. These characteristics are summarized in the table (Table 12.27), while the spread of properties is better illustrated by the graphs (Figure 12.29, Figure 12.30, Figure 12.31, Figure 12.32, Figure 12.33, Figure 12.34). 12.3.3 Additives The behavior of polypropylene can be extensively shaped and modified by the use of additives. Some of these modifications are essential and are present in all grades of polypropylene, particularly the use of antioxidants to prevent thermal degradation. Others are optional and are used to change the performance in

Table 12.27 Principal characteristics of polypropylene forms

Property

Best choice

Stiffness

Homopolymer

Resistance to high temperature

Homopolymer

Chemical resistance

Homopolymer

Surface hardness

Homopolymer

Impact strength

Block copolymer

Toughness

Block copolymer

strength at low temperatures

Block copolymer

Transparency

Random copolymer

Flexibility

Random copolymer

Sealability

Random copolymer

Figure 12.29 Polypropylene forms compared by


elongation at elastic limit as a function of flexural modulus. [1016]

notched Izod impact strength as a function of melt flow index. [1016]

Figure 12.30 polypropylene forms compared by

Figure 12.32 polypropylene forms compared by

flexural modulus as a function of tensile stress at the elastic limit. [1016]

brittleness temperature as a function of melt flow index. [1016]


Design principles

138 Table 12.28 Effect of form in fillers and reinforcements. [1157]

Fibers

Figure 12.33 Polypropylene forms compared by melting point as a function of flexural modulus. [1016]

Platelets

Spheres

glass, carbon

talc, mica

glass, calcium carbonate, barium sulfate

Tensile strength

Stiffness

Impact strength

Warping

Key: = increase

= decrease

= marginal

Table 12.29 Normal loading range for fillers and reinforcements in polypropylene.

Filler / Reinforcement Talc

Vicat softening point as a function of flexural modulus. [1016]

some specific desired aspect, for example to improve mechanical strength or increase resistance to combustion. Such improvements may well be accompanied by a deterioration in another aspect of material behavior. Polypropylene accepts additives well, and this ability to modify the material by such means plays a part in the outstanding versatility of polypropylene as a manufacturing material. Here we draw attention to those aspects of additives that are of particular significance to the designer. 12.3.3.1 Fillers and reinforcements The primary effect of fillers and reinforcements is to modify the mechanical properties of polypropylene. Side effects, both desirable and undesirable, may crop up in other performance areas of the compound. The effect of a reinforcement or filler depends to an extent on its physical form which can take the shape of a fiber, a platelet, or a sphere. For the purposes of classification, the term

Design principles

10–50

Calcium carbonate

10–60

Barium sulfate

20–50

Mica

10–50

Mineral, unclassified


Percentage loading by weight

5–45

Glass fiber

10–50

Glass fiber, coupled

10–40

Glass bead

10–40

Carbon fiber

10–40

sphere embraces three-dimensional granular forms as well as true spheres, while the term platelet refers to any essentially lamellar particle that is thin in relation to its area. The form of the additive has a bearing on the way in which it is incorporated into and interacts with the polymer chain, and this makes possible some broad predictions about the likely effect of fillers and reinforcements on polymer properties (Table 12.28). The terms filler and reinforcement are not precisely defined but reinforcement is generally understood to refer to fibrous forms while filler is taken to mean particulate matter (spheres, granules, platelets). Many fillers and reinforcements are imperfectly adapted for mixing and dispersion into plastics. Mineral additives particularly are characterized by a high surface area and highly polar nature that makes wetting and dispersion in the polymer difficult. To overcome this, reinforcements and fillers may be modified by means of surface treatments or coupling agents to make them more easily assimilated by the polymer. Surface treatments


139 aim to lower the surface energy and hence the attractive forces between the additive particles. Coupling agents on the other hand, act on the interface between additive and polymer to create or improve bonding between the two. Talc Talc is the most widely used filler for polypropylene and has the effect of improving stiffness, dimensional stability, heat distortion, and creep. A matt surface effect is usually displayed, and there is an adverse effect on impact strength and resistance to degradation by thermo-oxidation. Weldability is also reduced. Talc also acts as a nucleating agent. Talc filled polypropylene is used for: automotive under-hood applications, including cooling fans, air ducting, electrical housings other automotive applications, including fascia panels, headlight housings domestic appliances, including washing machine and tumble dryer components, kettle bodies, housings for irons and toasters, vacuum cleaner internal parts power tool housings lawn mower parts garden furniture Calcium carbonate Calcium carbonate has some advantages over talc as an additive for polypropylene. It can be chemically coupled, and is often given a surface treatment, for example with calcium stearate, to ensure good dispersion or to achieve high loadings. Compared with an equal loading of talc, polypropylenes filled with calcium carbonate have better impact strength, elongation at break, and surface quality but are inferior on tensile strength, stiffness, and heat distortion temperature. Calcium carbonate filled polypropylene is particularly used for: storage trays garden furniture camping toilets Glass fibers Glass fibers are widely used for reinforcing polypropylene. The effect is to improve tensile strength, flexural modulus, and dimensional stability, and to raise the heat distortion temperature. The drawbacks are reduced elongation at break, a reduction in electrical properties, and a tendency to distortion in injection moldings. Distortion arises from the flow orientation of reinforcing fi-


bers during melt processing. The orientation process is more complex than is generally imagined, and is not uniform throughout the thickness of the part. The end result though, is that any departure from a random orientation of fibers will result in anisotropic properties (properties that vary with the flow direction). It is this variation that tends to cause distortion. The effect of the glass fiber reinforcement can be considerably enhanced by the use of coupling agents that increase the bond between the fibers and the polypropylene matrix. The effect is to ensure a more efficient transfer of stress from the matrix to the fibers which are consequently more fully utilized. Polypropylenes reinforced with coupled glass fibers have greater stiffness and strength than uncoupled glass types (Figure 12.35, Figure 12.36, Figure 12.37). Typical applications of glass reinforced polypropylene include automotive under-hood applications and headlamp housings and washing machine components. The length and diameter of the fiber have a bearing on the reinforcing effect. These two considerations are coupled in the aspect ratio — the ratio of fiber length to diameter. The critical aspect ratio is that at which the loaded fiber would be subject to its ultimate tensile strength. The average fiber aspect ratio is usually at least ten times greater than the critical aspect ratio. The situation is complicated by the tendency of compounding and processing to reduce the fiber length by mechanical fracture. Studies show that fiber length after compounding and molding is almost independent of the initial length (Table 12.30). By reducing the fiber diameter, more fibers survive compounding and process-

Figure 12.35 Effect of 20% coupled and noncoupled glass fiber reinforcements on tensile strength of polypropylene. [1059]

Design principles

140

Figure 12.36 Effect of glass fiber reinforcement type and content on tensile strength of polypropylene. [1059]

ing with an aspect ratio above the critical value. For semi-crystalline thermoplastics as a whole, the evidence suggests that tensile strength can be improved by 6% to 10% by reducing the fiber diameter from 13 microns to 10 microns. Greater improvements can be produced by reinforcing polypropylene with long fibers (Figure 12.38). The pellets are produced by a pultrusion technique that eliminates the fiber damage caused by conventional extrusion compounding. Because the fibers are oriented for pultrusion, it is possible to produce glass loadings up to 75% compared with a practical limit of about 50% for compounded short fibers. The fiber length before proc-

Figure 12.37 Effect of glass fiber reinforcement type and content on heat deflection temperature of polypropylene. [1059]

essing is effectively the same as the pellet length, and is typically 10mm to 12mm. Fiber damage and fracture does still occur in processing, but studies show that the effect is much less than had been presumed. Long-fiber reinforced polypropylene challenges for markets currently held by polyamides and other engineering plastics reinforced with short fibers. The properties are comparable while the cost and weight advantage is substantial. Glass spheres Glass spheres or beads may be used alone as a re-

Table 12.30 Effect of polypropylene processing on reinforcing glass fibers. [1165]

Input strand length (mm)

Strand length after compounding (mm)

Strand length after injection molding (mm)

3.2

0.76

0.64

4.8

0.76

0.66

Figure 12.38 Improvement in polypropylene prop-

6.4

0.99

0.69

erties produced by long-fiber reinforcement compared with short fibers. [1161]

Design principles


141 inforcement but can be deployed in combination with glass fibers. The beads improve stiffness and compressive strength without imparting any directional characteristic. Consequently there is far less tendency for distortion compared with fiberreinforced grades. Other fillers and reinforcements Mica additives can be chemically coupled and surface treated to improve dispersion. They are usually employed to increase stiffness. Wood flour has been used to improve the acoustic property of polypropylene. Wollastonite, a silicate mineral, improves impact strength. Barium sulfate improves stiffness and acoustic property while having relatively little effect on surface finish. Asbestos fibers form a very effective reinforcing agent for polypropylene but the health risk involved in compounding as well as in processing and secondary operations means that the option is no longer available. 12.3.3.2 Nucleating and clarifying agents Polypropylene is a semi-crystalline material containing ordered crystalline regions that at room temperature typically make up about 60% of the total matter; the remaining material is amorphous. These crystalline regions scatter light passing through the material and the result is the familiar milky translucent appearance that we associate with polypropylene. Both nucleating and clarifying agents act on the crystalline regions to achieve their effects. The primary purpose of a nucleator is to produce a stiffer and faster-cycling polypropylene (Table 12.31), while the aim of a clarifier is to improve transparency. Transparency is particularly desirable in packaging applications. Nucleating agents cause the cystallline regions to start forming earlier at a higher temperature. The result is a faster and more complete degree of crystallization in which the regions are smaller and more uniform. This produces a polypropylene with increased stiffness and a slight reduction in impact strength. Some nucleating agents also improve the clarity of polypropylene. Moldings made from nucleated grades of polypropylene can safely be ejected from the mold at higher temperatures than standard grades, because of the truncation of the supercooled state. This of course means faster cycle times, but, paradoxically, fast-cycling thinwalled parts may not benefit from nucleation due


Table 12.31 Effect of nucleation on characteristics of polypropylene. [1064]

Standard polypropylene

Nucleated polypropylene

Crush resistance Impact resistance

Transparency of homopolymer Cycle time

Shrinkage, total

Moldability

Extrudability

Thermoformability Key: = better

= slightly better

= similar

to the risk of premature freezing and short shots in thin sections. Nucleating agents for polypropylene generally consist of sodium benzoate, kaolin, or talc. Some red pigments are known to interact with sodium benzoate and undergo a an unwanted color change. Random copolymers of polypropylene are naturally clearer than homopolymers and block copolymers, and are not normally nucleated because the effect is to reduce this clarity. Although clarifying agents also act as nucleators, they operate in quite a different way. Unlike nucleators, clarifiers melt and disperse in the polymer melt. The agents are transparent and have no supercooled phase, so they solidify at their melting point and by doing so they initiate crystallization of the polypropylene. Clarifying agents reduce the size of the crystalline regions, thereby reducing light scattering and increasing transparency. The transparency of the agents themselves also improves light transmission. The modification of crystal structure has the same effect on polypropylene properties and cycle times as a nucleator. Polypropylene clarifiers are generally derivatives of dibenzylidene sorbitol, and are subject to degradation if melt temperatures exceed 230°C. Degradation increases haze levels; in severe cases the polypropylene may be tainted in smell and taste, and specks may be present in the material. The agent may also form deposits on the mold. Some newer clarifying agents are appearing with a temperature tolerance extending to 260°C. Low processing temperatures can also be a problem. Transparency is reduced if temperatures are low enough (below about 195°C) to interfere with full dispersion of the clarifying agent. Anti-

Design principles

142 static agents are often used with clarifiers to assist in dispersion and to counteract any ejection problems arising from the higher freezing temperature. 12.3.3.3 Colorants In its untreated form, polypropylene is a translucent colorless material and consequently it is capable of being colored to virtually any desired shade. Color is defined in terms of shade, intensity and lightness, and is imparted by means of pigments or dyes. It is an obvious pre-requisite that the colorant must be stable at the melt processing temperature. The quantity required depends on the tinting strength of the colorant. Other considerations include light fastness, chemical compatibility with polypropylene, whether the colorant is suitable for food or medical use, and the health and safety aspects of the colorant itself. Pigments are insoluble organic or inorganic materials that are dispersed throughout the polypropylene matrix whereas dyes are organic materials that are soluble in the polypropylene. Dyes are easily dispersed throughout the material and result in a more transparent product. On the downside, dyes have a tendency to migrate and are more limited in heat stability and fastness to light. Pigments on the other hand, are available in a wide range of organic and inorganic types, and the chief difficulty is to disperse them evenly throughout the polypropylene. Incomplete dispersion results in agglomerations of pigment particles that cause streaks and uneven shades in the finished article. Organic pigments have more tinting strength and are generally brighter and more transparent than inorganic pigments. However, they are the hardest type to disperse. Organic pigments are generally superior in terms of heat stability and fastness to light. The dispersion problem, coupled with the need to use more than one colorant to create most shades, has resulted in a number of alternative strategies for coloring polypropylene. 12.3.3.4 Flame retardants Unmodified polypropylene ignites at a temperature of about 360°C and forms burning drips with the potential to spread fire. Flame retardant grades are available with increased fire resistance to V2 or V0 rating on the UL94 scale. The improvement is produced by flame retardant additives that have the dual effect of increasing resistance to ignition and reducing the spread of flame. Unfortunately, there is a severe downside to the use of flame re-

Design principles

tardants. High concentrations are needed to produce fire resistance and the resulting compound is generally unsuitable for food applications. Retardants substantially reduce the physical properties of polypropylene and generally impose a limit on the melt processing temperature which should not exceed 230°C. Many flame retardants will cause polypropylene integral or ‘living’ hinges to fail. 12.3.3.5 Blowing agents The function of a blowing agent is to generate a gas during melt processing and thereby to expand the polymer into a cellular structure or foam. Agents are classified as physical or chemical, depending on the way in which the gas is evolved. Physical blowing agents consist of gases that are held in solution in the polymer melt under pressure. When the melt pressure is partially relaxed, the gas comes out of solution. The usual gases are nitrogen and carbon dioxide. A variant of the physical blowing agent is a suitable volatile liquid that vaporizes to form a gas at melt processing temperatures. The chemical blowing agents are solid compounds that decompose at melt processing temperatures; the decomposition product is a gas, usually nitrogen. Not all chemical blowing agents are safe for use in food contact applications. Polypropylenes containing blowing agents can be processed by injection molding and extrusion into products with a density 3 as low as 0.6 g/cm . Injection moldings produced from polypropylene containing a blowing agent have a homogeneous and substantially smooth surface skin covering an internal cellular structure. The process is often referred to as structural foam. Extruded foamed sheet, film and tape can be stretched and thermoformed. Typical applications include beverage cups trays for meat products, decorative film and tape, strapping tape, and carpet backing yarn. 12.3.3.6 Other additives Polypropylene formulations may include a range of other additives to deal with specific problems such as static build-up, slip, block, and UV degradation. These impinge on the designer to a lesser extent but there is a need to be aware of the options. Polypropylene is prone to a build-up of static electric charges that attract dust, make sheets and bags stick together, and cause a spark danger in hazardous environments. Anti-static agents dissipate the static charge, usually by attracting molecules of water to the polypropylene surface. Most


143 anti-static agents work by migrating to the polymer surface where they can cause a problem with secondary operations such as printing. The difficulty can be overcome by common surface treatments including flaming and corona discharge. However, some non-migratory anti-static agents are available. The migratory types need time to work. Under normal conditions the optimum effect develops two to three days after processing but is then long-lasting and resistant to everyday washing and cleaning. Anti-static agents have a negligible effect on the mechanical, thermal, and chemical properties of polypropylene. Blocking is the tendency for an adhesive effect to develop between layers of film, particularly where they are under pressure in a stored reel. Slip or the lack of it is the phenomenon of high friction and slip-stick effects occurring between adjacent film layers. It can be a problem both in the manufacture of polypropylene articles and in their end use. Slip and anti-block agents are added to film grades of polypropylene to combat these effects. In outdoor exposure, polypropylene is susceptible to degradation by the ultraviolet (UV) spectrum of sunlight. The effect resembles that of oxidation and is evidenced by chalking and cracking of the surface, color change, and a reduction in properties. To counteract these effects, UV stabilizers are added to polypropylene compounds intended for outdoor exposure. Many are impaired by the presence of other additives or pigments. This means that it is unwise and undesirable for processors to attempt to further modify UV stabilized grades of polypropylene by compounding in other ingredients. Some UV stabilizers are unsuitable for contact with food although specially stabilized compounds are available for food service. The impact performance of polypropylene is improved by adding modifying co-monomers during polymerization but can also be adjusted by compounding in modifying elastomeric components. The usual modifier for polypropylene is EPDM rubber at loadings of 10% to 40% by weight. A secondary use of impact modifiers is to “restore” impact properties when these are adversely affected by other functional additives such as flame retardants. Impact modified polypropylenes are particularly used for automotive components, power tool housings, and blow molded containers.


12.3.4 Influence of metallocene technology A new generation of catalysts using metallocene technology is likely to have a great influence on polypropylene in the future. Metallocene catalysts are also known as single-site catalysts, although not all single-site catalysts are, strictly speaking, metallocenes. Development is very rapid and competitive in this area and it may be some time before the terminology settles down. The key point is that in comparison with conventional multi-sited catalysts, the metallocenes have the capacity to produce polymers with properties that were previously unattainable. Another advantage is that metallocene catalysts are homogeneous with, and are absorbed into the polymer product. The initial work has been done with polyethylene but a number of producers — Exxon, Hoechst, Fina, Dow, BASF — now have metallocene polypropylenes available in trial quantities. The new materials are becoming known in shorthand as mPP, and are characterized particularly by a very narrow distribution of molecular weight and a lower melting point (Table 12.32). Although the melting point is some 10°C below that of conventional polypropylene, the crystallization temperature is only about 5°C lower. A consequence of the narrow molecular weight distribution is a polymer with a low elongational viscosity and a low melt elasticity. These characteristics are particularly useful in extrusion where they reduce die swell and improve melt draw down for film and fiber operations. Other benefits include improved toughness and clarity better than that offered by nucleated or clarifier-additive grades of conventional polypropylene. Opinions are divided as to how rapidly metallocene polypropylene will attain commercial prominence. The material is beginning to be employed in fiber and film applications, but there seems to be some way to go before molding appliTable 12.32 Comparison of conventional and metallocene polypropylenes. [1137]

Metallocene polypropylene

Conventional polypropylene

2.0

3.5–6.0

0.01–5000

0.01–1000

Extractables

0.7%

3.3%

Melting point

147–158°C

160–165°C

Property Molecular weight distribution Molecular weight capability

Design principles

144 cations become significant. One industry authority believes that conventional catalysts will continue to dominate polypropylene molding materials for a further 5 to 10 years. Meanwhile, metallocene materials are emerging as additives and modifiers for conventional polypropylenes. Metallocene-based polyolefin plastomers and elastomers, or POPs and POEs as they are becoming known, are being used to improve the impact strength of polypropylene at low temperature. Another use is to inhibit radiation embrittlement in clarified polypropylene for medical applications. These metallocene-based additives reportedly cause no increase in haze when used with nucleated or clarified polypropylene grades. Other benefits include better weld line strength,

Design principles

easier flow, increased stiffness, lower shrinkage, and a reduction in thermal expansion. When used with glass reinforced polypropylene, the new additives can provide a balance of stiffness and impact strength that has hitherto been beyond the scope of polypropylene. It seems likely that the use of metallocene POP and POE modified polypropylene grades will develop rapidly both in niche markets and as alternatives to more highly priced polymers. References for chapter 12: [1004, 1012, 1016, 1032, 1038, 1049, 1057, 1059, 1063, 1064, 1101, 1102, 1103, 1106, 1137, 1148, 1157, 1158, 1159, 1161, 1162, 1165, 1174, 1175, 1216, 1218, 1219]


13 Processing fundamentals Processing overview Extrusion is the most widely practiced process for forming polypropylene, accounting for some 46% of consumption in the USA (Figure 13.1). Of this, the major share is taken by fiber and filament, two forms that are not readily identified with polypropylene in the public consciousness. Film, mainly for packaging and also not popularly recognized as polypropylene, is also a very significant extrusion product. Sheet and profile extrusion is of relatively minor importance. Almost one third of polyproUnspecified 23% Injection moulding 31%

Other extrusion 1% Sheet 2%

Blow moulding 2%

Film 12%

Fibre and filament 29%

Figure 13.1 Processing methods for polypropylene, USA, 1996. [1216]

pylene is processed by injection molding. Other processes such as blow molding, thermoforming, calendering and so on, probably account for less than 5% of polypropylene consumption. These figures are only a guide; almost a quarter of polypropylene is processed by unspecified methods. Nevertheless, the relative proportions of the various processing methods are probably reliable.

13.1 Properties influencing processing 13.1.1 Flow properties Polypropylene is formed into articles almost exclusively by melt processes that rely on the flow of the melted material at elevated temperatures. Injection molding, blow molding, extrusion, and thermoforming are all examples of melt processing. An understanding of melt flow is essential for success with these processes. The study of the flow of materials including that of polymers is known as rheology.


The rheology of a thermoplastics melt is complex, being very dependent on temperature and shear rate. This means that the melt viscosity — the characteristic that makes flow easy or difficult — can vary widely in the melt condition. The two key points about the flow of thermoplastics are that the behavior is non-Newtonian and that viscosities are very high. These characteristics are dictated by the long polymer chain molecular structure of the materials. One practical consequence is that considerable force is required to make a plastics melt flow into a mold or through a die. This explains why plastics processing machinery and molds must be so robust and are costly. To understand and control melt processes, it is necessary to define the way in which melt viscosity changes with temperature and shear rate. The shear rate is a measure of how fast the melt passes through a channel or orifice. A simple fluid such as water has a constant viscosity value regardless of shear rate. This is known as Newtonian behavior in which the fluid can be described fully by a single constant — the viscosity. By contrast, the viscosity of a plastics melt at a constant temperature changes markedly as the shear rate changes. This is non-Newtonian behavior. There is no single viscosity value. The viscosity value for a plastics melt must always be related to the shear rate at which it was determined and strictly it should always be referred to as the apparent viscosity, although this qualification is usually assumed rather than explicitly stated. An important consequence follows. For a viscosity value to be truly useful in determining how a process will turn out, it should be measured at about the same shear rate experienced in the process (Table 13.1). Unfortunately, this is not true of the most popular and widely available measure of melt viscosity, the melt flow rate (MFR) or melt flow index (MFI). Table 13.1 Process shear rate ranges Process

Shear rate

Injection molding

High

Blow Molding

Medium to low

Extrusion

Medium to high

Thermoforming

Medium to low

Melt flow rate testing

Low

Capillary rheometer testing

Medium to high

Processing fundamentals

146 Table 13.2 Approximate relationship between MFR and polypropylene injection molding conditions.

MFR range (g/10 min)

Injection pressure range (bar)

Melt temperature range (°C )

20

400–1000

200–230

The melt flow rate test is performed at a low shear rate so MFR figures will be at their least inaccurate for medium to low shear rate processes like blow molding and thermoforming, and will be most inaccurate for injection molding. The quoted MFR value is the weight of polymer melt flowing through an orifice in specified conditions, so the higher the MFR value, the lower the melt viscosity and the easier the material will flow (Table 13.2). Even though MFR values are measured at an unrealistically low shear rate, it might seem that the test would accurately rank different materials for comparative ease of flow. Unfortunately, not even this can be guaranteed because of the varying degree of shear dependency shown by different materials and grades. The MFR test owes its continued survival mostly to tradition and the fact that it is cheap and easy to perform. More reliable viscosity measurements can be made with high-shear rheometers. Material testing is performed at shear rates similar to those experienced during extrusion or injection molding, so the resulting values have a direct bearing on process

considerations (Figure 13.2). Even then, it is not a simple matter to depict flow behavior. A number of viscosity “models” have been developed to describe this behavior, and while a detailed discussion is beyond the scope of this work, it is as well to be aware of some of these models because they are used in process simulation computer programs that predict the effect of product and control parameters on the end product. The simplest version is known as the power law model. More elaborate and accurate models are based on higher order versions of the power law, or on the Carreau, Cross, or Ellis models. Flow data corresponding to these models is still not widely published but can usually be obtained on request from materials suppliers. Developers of flow simulation software maintain extensive databases of plastics flow data but these are not freely accessible. The situation is due to improve with the announcement that Campus, the free industrystandard materials database, will include rheological data in its next version. A third type of flow measurement is sometimes available, although its popularity appears to be waning. Spiral flow data is an attempt to relate flow information directly to the injection molding process by using an industrial molding machine to run the tests, in conjunction with a test mold in which a very long graduated flow channel is arranged in a spiral. The disadvantage is that reproducibility beTable 13.3 Approximate flow range of polypropylene compared with other thermoplastics.

Polymer

Approximate flow length for 2mm wall thickness (mm)

Polyamide 6/6

810

Polypropylene

250–700

LD polyethylene

550–600

Polyamide 6

400–600

PBT

250–600

HD polyethylene

200–600

Acetal

500

Polystyrene

200–500

PMMA

200–500

PET

200–500

Figure 13.2 Typical viscosity curves at 260°C for

Polyamide 12

200–500

some PCD polypropylene grades. Key: 1 = Daplen BHC 5003 (blow molding grade) — MFR 0.4, 2 = Daplen CF 501 (calender film grade) — MFR 1.1, 3 = Daplen FSC 1012 (block copolymer molding grade) — MFR 5.0, 4 = Daplen PT 551 (thin wall molding grade) — MFR 19.0.

ABS


320

PVC-U

160–250

Polycarbonate

150–220


147

Figure 13.3 Spiral flow length of some reinforced Hoechst polypropylenes at 750 and 1130 bar injection pressure Key: a = non-reinforced base grade, b = Hostacom M4 N01 (40% talc), c = Hostacom G2 N01 (20% glass fiber), d = Hostacom G3 N01 (30% coupled glass fiber).

tween different presses and molds is low. The spiral flow behavior of a thermoplastic is characterized simply by the flow length observed under prescribed conditions of temperature, pressure, and flow rate. Flow length measurements are specific to the test conditions and cannot be extrapolated to

other circumstances. For example, there is no straightforward way to relate flow data taken on a 2 mm thick test mold to a practical molding of a different thickness. However, because the test is performed at process shear rates, it will reliably rank materials for ease of flow at the test condition (Table 13.3). Practical considerations of time and cost make the test unwieldy for exposing temperature and shear dependencies (Figure 13.3). A wide spread of polymer chain lengths is an inevitable consequence of the polymerization process, and it is this that creates within any polymer a range of molecular weights. The statistical distribution of these molecular weights is known as the molecular weight distribution, or MWD. The sensitivity of polypropylene melt viscosity to shear and temperature is largely dependent on its molecular weight distribution. This distribution can be controlled to an extent so that polypropylene grades may be produced in broad or narrow molecular weight distributions (Figure 13.5). The broad MWD product will be more shear sensitive than a narrow MWD grade (Figure 13.6). This exposes another shortcoming of the melt flow rate test. Broad and narrow MWD polypropylenes can have the same

Figure 13.4 Approximate relationship between melt flow index and spiral flow length.



148

Figure 13.7 Effect of vis-breaking on the molecular weight distribution of polypropylene.

Figure 13.9 Melt viscosity behavior of controlled rheology polypropylene compared with conventional polypropylene. Key: BASF Novolen 100N = conventional homopolymer grade, BASF Novolen 1148 RCX = controlled rheology homopolymer grade.

Figure 13.8 Effect of vis-breaking on the melt viscosity and shear sensitivity of polypropylene.

melt flow rate and the same average molecular weight but still vary significantly in processing. Easier flowing grades of polypropylene can be produced by deliberately promoting chain scission during the production of the polymer. Chain scission involves a breaking of the polymer chains in a mechanism akin to degradation. Unlike degradation, the method results in a predictable and reproducible degree of chain scission. The result is a polypropylene with a narrower molecular weight distribution and a lower melt viscosity (Figure 13.7). The narrower molecular weight reduces the sensitivity of melt viscosity to shear, particularly at higher shear rates (Figure 13.8). Materials produced in this way are known as controlled rheology (CR) grades, or

sometimes as vis-broken (VB) grades (Figure 13.9). Homopolymers, random copolymers, and block copolymers are all available in controlled rheology versions. Controlled rheology grades of polypropylene are generally used for fiber and film production where the improved draw-down results in faster production rates, and for injection molding parts that are difficult to fill, or where it is important to minimize distortion or warpage (Table 13.4). 13.1.2 Thermal properties The melt processing of thermoplastics involves first heating the material to a point at which it can be made to flow, then cooling it again to a temperature at which the formed object is stable. This requirement constitutes a major energy demand in the forming process, and is central to the efficiency and economy of the process. It is a common perception that thermoplastics are difficult to heat and even harder to cool, and that this is particularly true of polypropylene. The perception is a

Table 13.4 Principal characteristics of controlled rheology polypropylenes Property

Advantage

Disadvantage

Narrower molecular weight distribution

Reduced warpage

Reduced melt strength

More uniform shrinkage

Reduced stiffness

Improved draw-down performance

Less reduction in viscosity at high shear rates

Shorter polymer chains


Reduced melt viscosity


149

specific heat (kJ/kg-K)

amides 6 and 6/6. It is more than double that of sound one, and a study of thermal characteristics polystyrene, and is considerably greater than the will show why this is so. energy requirement for materials with much higher The heat energy or heat content of a system is a melt temperatures, such as PPO, polycarbonate, and function of the mass of a material, its specific heat, PES. The cooling requirement for polypropylene is and the temperature change. The quantity is often even more severe. Only HD polyethylene is more referred to as enthalpy. The heat energy to melt a demanding. These thermal characteristics have a dithermoplastic is therefore proportional to the differrect bearing on processing. They mean for example ence between its melt temperature and room temthat cooling for a polypropylene mold must be perature. Theoretically, the heat energy to be remuch more efficient than for most other plastics. moved in cooling, in the case of a molding, is the difference between the melt temperature and the mold temperature. In practice, the component can usually be ejected at a higher temperature, and only a region near the surface 2.8 need be at this temperature, so the heat to be 2.4 extracted is considerably less. The heat energy involved in heating and 2.0 cooling varies considerably from one polymer 1.6 to another (Table 13.5). An additional consid1.2 eration is the fundamental difference between amorphous and semi-crystalline plastics. For 0.8 semi-crystalline materials, the heat require0.4 ment for melting includes an additional quantity for melting the crystalline structure. This 0.0 -150 -100 -50 0 50 100 150 is known as the latent heat of fusion of the temperature (°C) crystalline structure. At 670 J/g, the melting heat requirement of polypropylene is ex- Figure 13.10 Temperature dependency of specific heat of ceeded only by HD polyethylene and poly- polypropylene (PP) Table 13.5 Process heat requirements of polypropylene compared with other thermoplastics. Melt temperature (°C )

Mold temperature (°C )

Heat required to melt (J/g)

Heat removed on cooling (J/g)

PES

360

150

391

242

PET

275

135

556

305

Polystyrene

200

20

310

310

Acetal

205

90

555

345

Polycarbonate

300

90

490

368

ABS

240

60

451

369

PMMA

260

60

456

380

PPO

280

80

551

434

Polyamide 11

260

60

586

488

Polyamide 12

260

60

586

488

LD polyethylene

200

20

500

500

Polyamide 6

250

80

703

520

Polyamide 6/6

280

80

800

615

Polypropylene

260

20

670

670

HD polyethylene

260

20

810

810

Polymer



150 The need is often overlooked and it is this that is responsible for the commonly experienced difficulty of overheating cores and pins. The specific heat (Figure 13.10) and thermal conductivity of plastics vary greatly with temperature. So indeed does density. These variations are not brought out in data sheets that deal only with solid properties, and are not widely appreciated by plastics processors. It is still difficult to obtain information about the thermal properties of plastics in the melt state, even though this is important for plastics process calculations. A plot of enthalpy against temperature shows the extent of the variation and also clearly differentiates between amorphous and semi-crystalline materials. The enthalpy curve for the semi-crystallines shows a distinct discontinuity or “knee”. The rapid increase in enthalpy at this point corresponds to the latent heat of crystalline fusion. The curve for an amorphous materials shows no such discontinuity. The enthalpy curves give a direct read-out of the approximate heat energy to be added or removed when heating or cooling a plastics material, and deserve to be more widely distributed. The table (Table 13.6) gives guideline spot

Figure 13.11 Enthalpy of melt for some reinforced Hoechst polypropylenes. Key: a = non-reinforced base polypropylene, b = Hostacom M2 N01 (20% talc), c = Hostacom M4 N01 (40% talc), d = Hostacom G2 N01 (20% glass fiber), e = Hoechst Hostacom G3 N01 (30% coupled glass fiber).

Table 13.6 Approximate thermal melt properties of polypropylene compared with other thermoplastics.

Melt density (g/cm3)

Specific heat of melt (kJ/kg-K)

Thermal conductivit y of melt (W/m-K)

No-flow temperature (°C )

Freeze temperature (°C )

Latent heat of crystalline fusion (kJ/kg)

PES

1.48

1.3

0.15

240

225

0

PVC-U

1.15

1.5

0.14

120

85

0

PET

1.15

1.6

0.20

230

190

-

Polystyrene

0.88

1.8

0.13

130

95

0

Polycarbonate

1.01

1.8

0.19

180

150

0

SAN

0.92

1.9

0.15

140

100

0

PMMA

1.01

2.0

0.15

140

110

0

PPO

0.92

2.0

0.15

160

140

0

ABS

0.89

2.1

0.15

140

105

0

PBT

1.12

2.1

0.18

220

190

180

Acetal

1.22

2.5

0.13

150

140

0

Polyamide 6

0.95

2.7

0.12

220

215

200

Polyamide 6/6

0.97

2.7

0.13

250

240

250

Polypropylene

0.85

2.7

0.19

140

120

235

LD polyethylene

0.79

3.2

0.28

110

98

180

HD polyethylene

0.81

3.3

0.29

120

100

190

Polymer



151 values for the thermal properties of thermoplastics melts. In reality the values for density, specific heat, and thermal conductivity are temperaturerelated variables. The latent heat of crystalline fusion is zero for amorphous polymers because the phenomenon is absent. Freeze temperature is the point at which the material becomes a solid. The no-flow temperature is not a fundamental property. Rather it is a useful concept that has been introduced in flow calculations to compensate for shortcomings in viscosity models at low temperatures near to solidification. Effectively, it is the temperature at which the viscosity of a not quite frozen polymer is held to be infinite. Reinforcements and fillers tend to reduce the specific heat and enthalpy of polypropylene but the effect is not very great (Figure 13.11). If figures are not available for reinforced grades, it would be reasonable to use data for base grades which would then provide a small safety factor. Figure 13.12 PVT plot for Hoechst Hostalen PPN

13.1.3 Shrinkage and warping Shrinkage and warping are complex consequences of melt processing. For semi-crystalline plastics such as polypropylene the situation is particularly complicated. Crystalline regions exhibit a greater shrinkage than the surrounding amorphous regions, so semi-crystalline materials typically have a greater and more variable degree of shrinkage than amorphous materials. Plastics melts are compressible, particularly at the high pressures used in injection molding and extrusion. The fundamental property is the relationship between pressure, volume and temperature. Measurements describing this relationship for any material are known as PVT data, and are usually shown graphically in the form of a PVT plot. The plot for polypropylene (Figure 13.12) shows the now-familiar discontinuity or “knee” in the curve that corresponds to the region of crystalline fusion. PVT plots for amorphous materials by contrast reveal a simple change of slope at a point corresponding to the glass transition temperature. The PVT curves make it clear that shrinkage occurring as a result of melt processing is not just a function of thermal expansion and contraction but is also related to the compressibility of the melt. In practice, this relationship is made complex because process conditions will determine the extent to which the melt is compressed. Furthermore, process conditions are unlikely to be uniform throughout the part. Polypropylene shrinkage


1060 polypropylene homopolymer, measured during heating up.

is related to the degree of crystallinity in the material and hence to the cooling rate. A greater degree of crystallinity leads to a higher rate of shrinkage and also to a greater differential between shrinkage in the flow direction and shrinkage measured transversely to flow. The differential effect is another consequence of the visco-elastic property of long-chain molecules. During flow, the molecules are aligned to a limited extent in the flow direction and are extended to a degree proportional to shear rate. On cooling, a partial recovery of this extension gives rise to a higher shrinkage value. The effect is more pronounced in materials with a wide distribution of molecular weight. It is the differential shrinkage that is responsible for warping, the name given to the distortion of an apparently correctly formed part during and after cooling. A further difficulty is that shrinkage takes place over a period of time. In the case of an injection molding, the greater part of total shrinkage is evident virtually immediately after ejection from the mold but shrinkage will continue for more than 24 hours. During this time, further crystallization and relaxation of internal stresses result in small dimensional changes. Thereafter, further changes take place very slowly but the effect is dependent on temperature and will occur more rapidly if the part is exposed to elevated temperatures.


152

Figure 13.13 Shrinkage of some particulate-reinforced Hoechst polypropylenes. Key: a = non-reinforced base grade, b = Hoechst Hostacom M2 N01 (20% talc), c = Hoechst Hostacom M4 N01 (40% talc).

The sum of all these considerations means that it is impossible to state a simple and precise design figure for polypropylene shrinkage. Shrinkage can be minimized by using high viscosity, controlled rheology, or non-nucleated grade types. Warpage can be limited by using materials with a narrow Table 13.7 Approximate shrinkage range of polypropylene compared with other thermoplastics.

Figure 13.14 Shrinkage of fiber-reinforced polypropylenes. a) non-reinforced hose grade, b) 20% glass fiber, c) 30% glass fiber.

molecular weight distribution, particularly the controlled rheology types. Although it is a volumetric phenomenon, shrinkage is usually expressed as a linear quantity either as a percentage or as a linear ratio (mm per mm for example) (Table 13.7). The effect of fillers and reinforcements on shrinkage depends largely on the physical form of the additive. Particulate fillers such as talc or glass beads tend to counteract the effect of molecular orientation and so not only reduce shrinkage, but also reduce shrinkage differentials and hence the tendency to warp (Figure 13.13). Fibrous reinforcements also reduce shrinkage but because during flow the fibers become partially oriented, the reduction is much greater in the flow direction than in the transverse direction (Figure 13.14). This results in an increase in shrinkage differentials, although the increased tendency to warp is opposed to an extent by the greater stiffness of the reinforced material. In complex moldings, the varying flow patterns make it very difficult to anticipate shrinkage correctly by any means other than computer analysis. Even then, it is wise to design the product assembly to be tolerant of a degree of distortion and inaccuracy.

Shrinkage (%)

Shrinkage (mm/mm)

Range (%)

SAN

0.4–0.6

0.004–0.006

0.2

PPO

0.5–0.7

0.005–0.007

0.2

PES

0.6–0.8

0.006–0.008

0.2

Polycarbonate

0.6–0.8

0.006–0.008

0.2

ABS

0.4–0.7

0.004–0.007

0.3

Polystyrene

0.4–0.7

0.004–0.007

0.3

Polyamide 11

0.3–0.7

0.003–0.007

0.4

PVC-U

0.4–0.8

0.004–0.008

0.4

PET

1.6–2.0

0.016–0.020

0.4

PMMA

0.3–0.8

0.003–0.008

0.5

Polyamide 6

0.2–1.2

0.002–0.012

1.0

Polyamide 12

1.0–2.0

0.010–0.020

1.0

Acetal

1.5–2.5

0.015–0.025

1.0

13.2 Pre-processing

Polyamide 6/10

0.8–2.0

0.008–0.020

1.2

Polyamide 6/6

0.8–2.0

0.008–0.020

1.2

PBT

1.0–2.2

0.010–0.022

1.2

Polypropylene

1.2–2.5

0.012–0.025

1.3

HD polyethylene

1.5–3.0

0.015–0.030

1.5

LD polyethylene

1.0–3.0

0.010–0.030

2.0

Before any thermoplastic is processed into semifinished or end products, and irrespective of the process to be adopted, there are a number of prior considerations to be taken into account. For polypropylene, the principal questions are those concerning drying (13.2.1), coloring (13.2.2), and health and safety precautions (13.2.3).

Polymer



153 13.2.1 Drying Polypropylene has a very low tendency to absorb water and will not normally require drying before processing. If any moisture is present, it will be as water condensed or adsorbed on the polypropylene surface. This can occur, for example, if polypropylene is moved from a relatively cool store to a warm and humid environment in the processing shop. Because the effect is purely a surface one, the moisture can be easily removed by conventional dryers but of course it is better to avoid the problem by attending to the storage conditions. A simple hopper dryer will usually be sufficient to remove surface moisture from polypropylene granules. However, if the material is in the form of powder, the problem will be more severe, simply because of the greatly increased surface area available for adsorption. Powdered materials constitute an explosion hazard and should not be dried in conventional equipment intended for granules. Instead, the problem should be circumvented by storing producer-dried powders in sealed containers at equable temperatures. Certain carbon black or flame retardant grades of polypropylene have a somewhat increased tendency to attract moisture if stored for long periods in a damp atmosphere. In this case, drying should be performed at 105°C to 120°C for 1 to 3 hours. This treatment can also be applied to all polypropylene grades should hopper drying prove inadequate or be unavailable. 13.2.2 Coloring Polypropylene is an essentially colorless material, ranging from milky white to near transparent depending on form and type. This characteristic means that it is possible to color the material to almost any desired shade by the inclusion of suitable dyes or pigments. The quality of the end result depends crucially on the even and thorough dispersion of the colorant throughout the polypropylene melt, and processors have a variety of means at their disposal for achieving this. Coloring operations can be broadly divided into those that are coincidental with the forming process (inprocess coloring) and those that precede it (preprocess coloring). Pre-process coloring (13.2.2.1) involves a separate coloring operation that takes place before the primary forming process. The method gives very good results but is relatively costly and adds to the heat history of the material. In-process coloring


methods are, as the name implies, carried out during and as an integral part of the primary forming process. These processes — injection molding, blow molding, extrusion — involve the use of an extruder screw as a melt plasticizer, and it is this that is pressed into service for the additional duty of dispersing a colorant additive throughout the melt. The process screws are not designed expressly for this duty and cannot be optimized for it. Instead, the machine designer has to compromise to produce a screw and barrel that will work well enough with a range of polymers, while providing a reasonable balance between the conflicting requirements of throughput, heat transfer, mixing, pressure, and cost. Process conditions too, must be a compromise between what is best for dispersion and what is best for the physical product. Consequently, the principal worry with inprocess coloring is how to achieve widespread, uniform, and repeatable dispersion of color additives. Mixing can be improved by the addition of simple static mixers such as screen packs or flow-divider nozzles, but at the cost of greater process pressure drops and perhaps reduced throughput. On the plus side, no additional heat history is imparted to the material, and the equipment, energy, and time is effectively free. The processor also has no need to hold large inventories of bulk colored material, and can respond rapidly to changing needs and specifications. The three common methods of in-process coloring are color concentrate (13.2.2.2), liquid color (13.2.2.3), and dry color (13.2.2.4). 13.2.2.1 Color-compounded material Color-compounded polypropylene comes to the processor already colored in standard or custom colors. These materials are produced either by the polypropylene manufacturer or more commonly by a specialist compounder. The color is added in a melt process, generally a continuous process using an extruder or a screw-based compounder. Batch wise processes can also be performed with internal or roll mixers but are less convenient and uniform for thermoplastics. The color compounding process concludes with a pelleting operation that results in colored granules ready for use in injection molding, extrusion, and other forming processes. The compounding equipment can be optimized for mixing, so the colorants are uniformly and widely dispersed throughout the material. Together with the availability of specialist color formulation and color measuring equipment, this


154 gives consistent and high quality results but there are a number of disadvantages. Polypropylene is prone to oxidation at melt temperatures and must be stabilized to counteract this. By imposing an extra melt operation, the color compounding process adds to the thermal strain or as it is often known, the heat history of the material. The additional operation also adds an extra cost which is partially offset by the efficiency gains of a dedicated business. Standard color ranges are necessarily limited, and the minimum order quantity for custom colors may be high. Color-compounded materials are used by the processor in exactly the same way as natural grades of polypropylene. Color dispersion is already complete, so process conditions and equipment need take no account of this consideration. The color shade of the finished article can be taken for granted, provided quality checks are performed on the incoming compound. Minor process parameter adjustments may be necessary when changing from natural to color-compounded material but this is just a function of the minor rheological and thermal effects of the color additive on the polypropylene matrix. 13.2.2.2 Color concentrate or masterbatch Color concentrate combines some of the advantages of pre-process and in-process coloring. The color concentrate is a thermoplastic compounded in the pre-process manner with a very high loading of colorant. It is then added in a minor proportion to natural (uncolored) polypropylene, and the process plasticizing screw has the task of mixing and distributing the colored polymer proportion throughout the mass of natural material. This requirement is relatively unexacting because the primary task of dispersion has already been performed during manufacture of the color concentrate. Consequently, there should be no chance of color agglomerates forming, even if the process screw is a relatively inefficient mixer. The degree of dilution, or in other words the proportion of concentrate added to the polypropylene to be colored, is known as the let-down ratio. The concentrate manufacturer will aim to get the ratio as large as possible, but it is limited by the mixing efficiency of the conversion machinery and by the practicalities of concentrate compounding. Color concentrate is now the most widely used method of coloring polypropylene. The processor requires only simple metering equipment to con-


trol the let-down ratio, and the added heat history is negligible. On the downside, the carrier polymer used in production of the color concentrate may have a minor effect on processing and on the properties of the finished part. This is because the carrier for a polypropylene color concentrate is unlikely to have exactly the same characteristics as the grade being colored. Indeed, the carrier may well be of polyethylene rather than polypropylene. These differences arise from the economic and logistical need to produce a near-universal color concentrate. The effects are usually insignificant provided the let-down ratio remains large. 13.2.2.3 Liquid color Liquid color has not achieved the popularity among processors that it once promised, perhaps because of the need to retro-fit metering pump equipment to the process machinery. The method is probably best suited to long runs of a particular color. The colorants are dispersed in a liquid carrier base to form an ink-like material which is pumped into the entry of the plasticizing screw at a metered rate proportional to the throughput of polymer. Both the initial dispersion of colorants in the carrier, and the secondary mixing with the natural polypropylene are relatively easy because of the low viscosity of the liquid color. This also makes it possible to use very high let-down ratios that help to minimize the effect of the carrier on the processing and finished properties of the product. Cleaning, color changes, and spills are more troublesome to deal with than is the case for color concentrates. 13.2.2.4 Dry color Once the most popular method with injection molders, dry color has now been displaced by color concentrates. The method appears simple but is the one most likely to result in inadequate color dispersion and shift-to-shift irregularities. The color additive in the form of a powder is initially distributed in the polymer solid phase rather than the melt phase. This is done by mixing dry color with polypropylene granules in mechanical blending equipment such as tumble or ribbon blenders. The aim is to coat the granules evenly with color particles, and additives may be used to promote the distribution and adhesion of the particles. Among the many disadvantages are the need to handle hazardous dusty materials, the high survival rate of unbroken color agglomerates, the dif-


155 ficulty of cleaning the equipment, and the likelihood of inadequate color quality assurance and control. The color-coated granules are subsequently processed in conventional machinery, where the plasticizing screw has the exacting duty of wetting the color particles with the plastics melt and then dispersing them evenly throughout the mass. The task is at the outer limit of the mixing capability of melt process plasticizing systems and results rarely match the quality and uniformity of those obtained by the other coloring methods. 13.2.3 Safety precautions Polypropylene is an intrinsically safe and nontoxic material, and when correctly processed no harmful vapors should be formed. Nevertheless, it is good practice to ventilate process workplaces. This is particularly true when processing flame retardant grades or when the material is exposed at high temperatures to the atmosphere, as it is for example in film extrusion. The material is combustible at 345°C to 360°C and forms molten burning droplets that may spread the fire, so polypropylene processing plants should be equipped with fire precautions to the appropriate local standard. Water, powder and CO2 extinguishers can be used in the event of a fire, and a mask should be worn to prevent the inhala-

tion of combustion fumes. Burning polypropylene will stick to the skin and cause severe burns so protective clothing and particularly gloves are necessary when tackling a fire. Polypropylene is normally supplied in the form of granules that do not present an explosion hazard. However, finely divided polypropylene in the form of dust or powder does, like many other materials, create a risk of explosion. Transportation and handling systems should be designed to minimize dust formation, and should be cleaned regularly to prevent dust accumulations. Powdered polypropylene should be subject to the precautions required for other flammable explosive dusts. The movement of granules during discharge from bulk containers is likely to generate static charges that may cause shocks and sparks, and may interfere with electronic equipment. Silos and bins should be earthed to prevent this. Polypropylene producers supply materials safety data sheets (MSDS) that summarize the risks precautions to be observed when working with the material (Figure 13.15) References for chapter 13: 1004, 1012, 1016, 1032, 1049, 1057, 1059, 1063, 1101, 1102, 1106, 1150, 1151, 1153, 1154, 1156, 1183, 1216, 1220

Figure 13.15 Typical materials safety data sheet for polypropylene.

EXXON CHEMICALS -- ESCORENE POLYPROPYLENE MATERIAL SAFETY DATA SHEET FSC: 6850 NIIN: 00N018142 Manufacturer's CAGE: 29700 Part No. Indicator: A Part Number/Trade Name: ESCORENE POLYPROPYLENE =========================================================================== General Information =========================================================================== Company's Name: EXXON CHEMICALS CO Company's P. O. Box: 3272 Company's City: HOUSTON Company's State: TX Company's Country: US Company's Zip Code: 77001 Company's Emerg Ph #: 713-656-3424;800-424-9300(CHEMTREC) Company's Info Ph #: 713-656-2443 Record No. For Safety Entry: 001 Tot Safety Entries This Stk#: 001 Status: SMJ



156

Date MSDS Prepared: 24FEB89 Safety Data Review Date: 18DEC91 MSDS Serial Number: BLXSP Hazard Characteristic Code: N1 =========================================================================== Ingredients/Identity Information =========================================================================== Proprietary: NO Ingredient: PROPENE POLYMERS; (POLYPROPYLENE). PEL:15 MG/M3 TDUST;5 MG/M3 RDUST. PEL & TLV AS PARTICULATES NOT OTHERWISE REGULATED. Ingredient Sequence Number: 01 NIOSH (RTECS) Number: UD1842000 CAS Number: 9003-07-4 OSHA PEL: SEE INGRED NAME ACGIH TLV: 10 MG/M3 TDUST =========================================================================== Physical/Chemical Characteristics =========================================================================== Appearance And Odor: CLEAR TO OPAQUE, WHITE (OR COLORED) SOLID PELLETS OR GRANULES. Boiling Point: N/A Melting Point: >225F,>107C Vapor Pressure (MM Hg/70 F): NEGLIGIBLE Specific Gravity: 0.88 Evaporation Rate And Ref: NOT APPLICABLE Solubility In Water: INSOLUBLE =========================================================================== Fire and Explosion Hazard Data =========================================================================== Flash Point: >600F,>316C Lower Explosive Limit: N/A Upper Explosive Limit: N/A Extinguishing Media: WATER SPRAY. Special Fire Fighting Proc: USE H&2O SPRAY TO COOL FIRE EXPOS SURF & TO PROT PERS. ISOLATE FUEL SUPPLY FROM FIRE. WEAR NIOSH/MSHA APPRVD SCBA & FULL PROT EQUIP (FP N). Unusual Fire And Expl Hazrds: SOLID MATL MAY BURN @/ABOVE FLASHPOINT & AIRBORNE DUST MAY EXPLODE IF IGNITED. TOX GASES WILL FORM UPON COMBUSTION. STATIC DISCHARGE MATL CAN ACCUM (SUPP DATA) =========================================================================== Reactivity Data =========================================================================== Stability: YES Cond To Avoid (Stability): TEMPS OVER 480F MAY CAUSE RESIN DEGRADATION. Materials To Avoid: NONE SPECIFIED BY MANUFACTURER. Hazardous Decomp Products: OXYGEN-LEAN CONDITIONS MAY PRODUCE CARBON MONOXIDE & IRRITATING SMOKE. Hazardous Poly Occur: NO Conditions To Avoid (Poly): NOT RELEVANT.



157

=========================================================================== Health Hazard Data =========================================================================== LD50-LC50 Mixture: NONE SPECIFIED BY MANUFACTURER. Route Of Entry - Inhalation: YES Route Of Entry - Skin: NO Route Of Entry - Ingestion: NO Health Haz Acute And Chronic: EYE:PARTICULATES MAY SCRATCH SURF/CAUSE MECH IRRIT. SKIN:EXPOS TO HOT MATL MAY CAUSE THERMAL BURNS. NEGLIGIBLE HAZARD @ AMBIENT TEMP. INHAL:NEGLIGIBLE HAZARD @ AMBIENT TEMP. VAPS AND/OR AEROSOLS WHICH MAY BE FORMED @ ELEVATED TEMPS MAY BE IRRIT TO EYES & RESP TRACT. INGEST:MINIMAL TOXICITY. Carcinogenicity - NTP: NO Carcinogenicity - IARC: NO Carcinogenicity - OSHA: NO Explanation Carcinogenicity: NOT RELEVANT. Signs/Symptoms Of Overexp: SEE HEALTH HAZARDS. Med Cond Aggravated By Exp: NONE SPECIFIED BY MANUFACTURER. Emergency/First Aid Proc: EYE:IMMED FLUSH W/POTABLE WATER FOR MINIMUM OF 15 MIN, SEEK ASSIST FROM MD (FP N). SKIN:FOR HOT PROD, IMMED IMMERSE IN/ FLUSH AFFECTED AREA W/LG AMTS OF COLD H2O TO DISSIPATE HEAT. COVER W/CLEAN COTTON SHEET/GAUZE & GET MD IMMED. NO ATTEMPT SHOULD BE MADE TO REMOVE MATL FROM SKIN/TO REMOVE CONTAM CLTHG, AS DAMAGED FLESH CAN EASILY BE TORN. INHAL:IMMED REMOVE AFFECTED VICTIM FROM EXPOS. (SUPP DATA =========================================================================== Precautions for Safe Handling and Use =========================================================================== Steps If Matl Released/Spill: RECOVER SPILLED MATERIAL & PLACE IN SUITABLE CONTAINERS FOR RECYCLE OR DISPOSAL. Neutralizing Agent: NONE SPECIFIED BY MANUFACTURER. Waste Disposal Method: CONSULT EXPERT ON DISPOSAL OF RECOVERED MATL & DISPOSE OF I/A/W FEDERAL, STATE & LOCAL REGULATIONS. Precautions-Handling/Storing: NONE SPECIFIED BY MANUFACTURER. Other Precautions: NONE SPECIFIED BY MANUFACTURER. =========================================================================== Control Measures =========================================================================== Respiratory Protection: WHERE CONCENTRATIONS IN AIR MAY EXCEED LIMIT GIVEN, WORK PRACTICE OR OTHER MEANS OF EXPOSURE REDUCTION ARE NOT ADEQUATE. NIOSH/MSHA APPROVED RESPIRATORS MAY BE NECESSARY TO PREVENT OVEREXPOSURE BY INHALATION. Ventilation: LOC EXHAUST VENT OF PROCESS EQUIP MAY BE NEEDED TO CONTROL PARTICULATE EXPOSURES TO BELOW RECOMMENDED EXPOSURE LIMIT. Protective Gloves: THERMAL RESISTANT GLOVES. Eye Protection: CHEM WORK GOG & FULL LENGTH FSHLD(FP N). Other Protective Equipment: ARM PROTECTION. Work Hygienic Practices: NONE SPECIFIED BY MANUFACTURER. Suppl. Safety & Health Data: EXPLO HAZ:STATIC CHARGES WHICH CAN CAUSE INCENDIARY ELEC DISCHARGE. FIRST AID PROC:ADMIN ARTF RESP IF BRTHG IS STOPPED. KEEP @ REST. CALL FOR PROMPT MED ATTN. INGEST:CALL MD IMMED (FP N)



158

=========================================================================== Transportation Data =========================================================================== Trans Data Review Date: 92065 DOT PSN Code: ZZZ DOT Proper Shipping Name: NOT REGULATED BY THIS MODE OF TRANSPORTATION IMO PSN Code: ZZZ IMO Proper Shipping Name: NOT REGULATED FOR THIS MODE OF TRANSPORTATION IATA PSN Code: ZZZ IATA Proper Shipping Name: NOT REGULATED BY THIS MODE OF TRANSPORTATION AFI PSN Code: ZZZ AFI Prop. Shipping Name: NOT REGULATED BY THIS MODE OF TRANSPORTATION Additional Trans Data: NOT REGULATED FOR TRANSPORTATION =========================================================================== Disposal Data =========================================================================== =========================================================================== Label Data =========================================================================== Label Required: YES Technical Review Date: 18DEC91 Label Date: 18DEC91 Label Status: G Common Name: ESCORENE POLYPROPYLENE Chronic Hazard: NO Signal Word: CAUTION! Acute Health Hazard-Slight: X Contact Hazard-Slight: X Fire Hazard-Slight: X Reactivity Hazard-None: X Special Hazard Precautions: COMBUSTIBLE. ACUTE: PARTICULATES MAY SCRATCH SURFACE/CAUSE MECHANICAL IRRITATION TO EYES. VAPORS AND/OR AEROSOLS WHICH MAY BE FORMED AT ELEVATED TEMPERATURES MAY BE IRRITATING TO EYES AND RESPIRATORY TRACT. MINIMAL TOXICITY IF SWALLOWED. CHRONIC: NONE LISTED BY MANUFACTURER. Protect Eye: Y Protect Skin: Y Protect Respiratory: Y Label Name: EXXON CHEMICALS CO Label P.O. Box: 3272 Label City: HOUSTON Label State: TX Label Zip Code: 77001 Label Country: US Label Emergency Number: 713-656-3424;800-424-9300(CHEMTREC) =======================================================================



14 Injection molding Introduction Almost a third of polypropylene consumption is processed by means of injection molding. The process produces a complex finished part in a single rapid and automatic operation. It is this that distinguishes plastics injection molding from most other manufacturing processes, although there are parallels with metal casting, and particularly with diecasting. Generally speaking, it would need a whole series of forming, joining, and finishing operations to replicate an injection molded article in other materials using different manufacturing methods. It is this point alone that makes injection molding economically viable. Injection molding machines and molds are very costly due to the high pressures needed to inject thermoplastics and the complexity of the necessary process controls. It is only the ability to produce a completely finished part at high speed that balances the equation and makes the injection molded article highly cost effective. Injection molded polypropylene parts are a familiar part of everyday life. In the home, they can be found in household appliances, kitchen equipment, in containers and caps, toys, and in the frames and shell of chairs. On the road, they are a key feature of the modern automobile in the form of fenders, fascias, trims, wheel well liners, and housings. In healthcare, injection molded polypropylene is the material of choice for disposable syringes. At work, they can be found in office equipment, crates and cases, and paint pots. Other familiar uses include food containers, video cassette boxes, and luggage.

14.1 The process The principle of injection molding is very simple. The plastics material is heated until it becomes a viscous melt. It is then forced into a closed mold that defines the shape of the article to be produced. There the material is cooled until it reverts to a solid, then the mold is opened and the finished part is extracted. Although the principle may be simple, the practice of injection molding is anything but simple. This is a consequence of the complex behavior of plastics melts and the ability of the process to encompass complicated products.


The essential mechanisms of injection molding are heat transfer and pressure flow. The essential equipment is an injection molding machine, sometimes known as a press, and a mold which may also be referred to as a tool or sometimes a die. The product of the process is a molding which confusingly and inaccurately is sometimes called a mold.

14.2 Injection molding machinery The are many varieties of injection molding machines, but they all perform the same essential functions. These are melting or plasticizing the plastics material, injecting it into the mold, holding the mold closed, and cooling the injected material. It is convenient to think of an injection molding machine as consisting of two units. The plasticizing and injection requirements are combined in the injection unit while the mold handling is performed by the clamp unit. The two units are mounted on a common machine base and are integrated by power and control systems. The convention is that the injection unit shall be on the right of the operator, with the clamp unit on the left (Figure 14.1). 14.2.1 Clamp unit The function of the clamp unit is to open and close the mold halves and particularly to hold the mold closed during injection of the plastics melt. High injection pressures are necessary, due to the high viscosity of plastics melts, so the force needed to hold the mold closed is very great. The melt pressure inside the mold is exerted over the entire area of cavities and feed systems at the mold parting line. The significant figure is the extent of this area

Figure 14.1 Typical injection molding machine.

Injection molding

160

Figure 14.2 Average mold pressure as a function of wall thickness for BASF Novolen1100L polypropylene homopolymer at 230°C.

when projected on to a plane perpendicular to the opening axis of the clamp system. This is known as the projected area of the mold. The clamp force needed to hold the mold shut during injection is a function of the injection pressure and the projected area, but this is not a simple function. The injection pressure varies throughout the cavities and feed systems and is also a complex function of process parameters such as melt and mold temperature, and injection rate. The cavity pressure is also a function of part thickness (Figure 14.2) which is completely independent of projected area, so attempts to determine clamp force on the basis of projected area are sure to be inaccurate. The means that the old ruleof-thumb method of allotting x units of clamp force per unit of projected area should be seen as a last resort. It is one that is likely to lead to under utilization of machines due the need for a large safety factor to cover the deficiencies of the method. The rule-of-thumb clamp figure for polypropylene is 2

to 4 tons per square inch of projected area. More reliable methods of determining clamp force are discussed in section 14.4.2. Clamp units range up to 3,000 tonnes closing force and more. The force requirements ensure that the clamp unit must be engineered very robustly, but this conflicts with the need to open and close the mold rapidly to minimize production time. A variety of clamp mechanisms has evolved in the search for a suitable compromise. The two most common types are the direct hydraulic clamp (Figure 14.3) and the toggle clamp (Figure 14.4). Other variants include hybrid toggle/hydraulic types, lock-and-block systems, and electro-mechanical systems. Whatever the variations, the clamp unit always features a stationary or fixed platen and a moving platen on which the mold halves are bolted or otherwise attached. The fixed platen is mounted rigidly on the machine base and is positioned adjacent to the nozzle of the injection unit. The injection half of the mold is attached to the fixed platen while the moving platen carries the ejection half of the mold. These terms may in the case of some sophisticated molds cease to be literally true, and the expressions fixed and moving mold halves are often used instead. The clamp also includes a tailstock platen or equivalent unit that the pressure means reacts against in order to clamp the mold halves together between the moving and fixed platens. For this purpose, the fixed and tailstock platens are united by tiebars (tie rods) that also serve as guides for the moving platen. The tiebars are stretched elastically when the clamp unit locks the mold shut under pressure. The tiebars limit access to the mold area and impede mold changing, and it is to overcome this that tiebarless machines have been intensively developed in recent years. The tiebarless machine uses the same clamp concepts but employs a greatly strengthened machine base to tie the fixed and tail-

Figure 14.3 Typical direct hydraulic clamp unit. A-Actuating plunger, B-Removable spacer, C-Mold, D-Injection nozzle, E-Fixed platen, F-Movable platen, G-Tie bar, H-Cylinder base plate, I-Clamping cylinder.

Injection molding

Figure 14.4 Typical toggle clamp unit. A-Movable platen, B-Fixed platen, C-Mold, D-Front link, E-Rear link, F-Actuating Cylinder, G-Tie bar, H-, I-Crosshead link.


161 14.2.2 Injection unit The function of the injection unit is to heat the plastics material to a uniform and homogeneous melt and to inject it into the mold under controlled conditions of pressure and flow rate. Given the low thermal conductivity, high specific heat, and high melt viscosity of thermoplastics, these are exacting tasks. Once again, many variants have been devised to solve the difficult problems involved. The variants can be grouped roughly into four principal injection unit concepts: single-stage ram or plunger two-stage ram single-stage screw two-stage screw/ram The single-stage ram unit is inefficient in heating, mixing and pressure transmission and is largely obsolete although the form survives in very small machines and some specialized equipment. It has the merit of simplicity and low cost. The two-stage ram is also all but obsolete. It was an attempt to improve on the single-stage ram by

stock platens together. The result is a completely unencumbered mold area with free access for automation, ancillaries, and mold changing operations. Under clamp pressure, the machine frame and platens flex elastically. Tiebarless machines use a variety of means to counteract this tendency and keep the platens parallel. However, the effect limits the clamp force that can be designed into tiebarless machines although the figure is gradually being pushed upwards. Currently the limit is about 400 tonnes. Another recent development, particularly in large injection molding machines, is a move towards two-platen clamp systems. These systems do away with the tailstock platen and use a variety of mechanisms to lock the tiebars to the moving platen in the closed position. The advantage of a twoplaten clamp is a considerable saving of up to 35% in floor space. Clamp units are rated according to the maximum closing force they can apply to the mold. The figure may be expressed as kiloNewtons (kN), metric tonnes (tonne) or US tons (ton) (Table 14.1). Table 14.1 Clamp force conversion table Nominal value (tonne)

Equiv. Value (ton)

Equiv. Value (kN)

25

27.6

245.2

50

55.1

75

Equiv. Value (tonne)

Equiv. Value (kN)

Equiv. Value (tonne)

Equiv. Value (ton)

25

22.7

222.4

250

25.5

28.1

490.3

50

45.4

444.8

500

51.0

56.2

82.7

735.5

75

68.0

667.2

750

76.5

84.3

100

110.2

980.7

100

90.7

889.6

1000

102.0

112.4

150

165.3

1471.0

150

136.1

1334.5

1500

153.0

168.6

200

220.5

1961.3

200

181.4

1779.3

2000

203.9

224.8

250

275.6

2451.7

250

226.8

2224.1

2500

254.9

281.0

300

330.7

2942.0

300

272.2

2668.9

3000

305.9

337.2

350

385.8

3432.3

350

317.5

3113.8

3500

356.9

393.4

400

440.9

3922.7

400

362.9

3558.6

4000

407.9

449.6

450

496.0

4413.0

450

408.2

4003.4

4500

458.9

505.8

500

551.2

4903.3

500

453.6

4448.2

5000

509.9

562.0

600

661.4

5884.0

600

544.3

5337.9

6000

611.8

674.4

700

771.6

6864.7

700

635.0

6227.5

7000

713.8

786.8

800

881.8

7845.3

800

725.7

7117.2

8000

815.8

899.2

1000

1102.3

9806.7

1000

907.2

8896.4

10000

1019.7

1124.0

1500

1653.5

14710.0

1500

1360.8

13344.7

15000

1529.6

1686.1

2000

2204.6

19613.3

2000

1814.4

17792.9

20000

2039.4

2248.1

2500

2755.8

24516.6

2500

2268.0

22241.1

25000

2549.3

2810.1

3000

3306.9

29420.0

3000

2721.6

26689.3

30000

3059.2

3372.1


Nominal Value (ton)

Nominal value (kN)

Injection molding

162

Figure 14.5 Typical reciprocating screw injection unit.

screw options for PVC and elastomers. Other options may include a so-called marbleizing screw for producing colored marble effects and a vented screw which includes a decompression zone and an associated exhaust port for the removal of water vapor or other volatiles. The practice is growing of offering two versions of the general-purpose screw for use with “commodity” or [1221] “engineering” plastics. Most general-purpose screws take the form of a single constant-pitch flight that decreases in depth from the input or upstream end to the output or downstream end (Figure 14.6). The flight pitch is usually equal to the screw diameter, giving a helix angle of 17.8°. Flight depth is usually substantially constant in the feed and metering zones and decreases at a constant rate over the compression zone. The feed zone typically occupies half the screw length, with the compression and metering zones each making up a quarter of the length. The key parameters of such a screw are the ratio of length to diameter (the L/D ratio), and the compression ratio. The L/D ratio affects mixing and melt uniformity, higher values giving better results. An L/D ratio of 20:1 is regarded as a minimum for injection molding. Screws as long as 28:1 are offered by some manufacturers. The compression ratio has a bearing on mixing and shear heating. Typical values range from 2:1 to 3:1 or greater. It is this parameter that varies between “commodity” and “engineering” general-purpose screws. The terms are inexact and the real difference is between semicrystalline and amorphous polymers. On heating to melt temperature, semi-crystalline materials undergo a greater volume increase than amorphous materials and so require a lower compression ratio.

separating the functions of heating and pressure flow, but the ram remains an inefficient mixer and heater. The two-stage screw/ram unit also separates the functions of heat and flow, using a screw for heating and mixing, and a ram for injection. Both are relatively efficient devices for their respective duties so the concept is attractive. However, the unit cost is higher, and it is difficult to devise an ideal melt flow path between the stages. The single-stage screw concept is by far the dominant form. A screw capable of both rotational and axial movement combines heating and mixing with the function of injection. For this reason, the form is frequently referred to as a reciprocating screw injection unit (Figure 14.5). The extruder-like screw operates within a heated barrel and has axial zones that are concerned successively with feeding, melting, and metering the plastics material. Many different screw forms have been designed in the search for the best compromise between plasticizing and throughput, particularly in recent years when CNC machining has made it possible to cut shapes that were previously impractical. The design process has been accelerated by extrusion simulation software that makes it possible to predict how a screw design will perform. Ideally, the screw should be optimized for use with a particular polymer, but this can only happen if it is known that the injection molding machine will be dedicated throughout its life to a narrow range of uses. Instead, virtually all injection molding machines are supplied with a screw that is designed as a compromise between the requirements for the majority of thermoplastics. This is known as a general14.6 Features of a typical injection screw. Key: L = screw length, purpose screw. It is usual for a ma- Figure D = diameter, h = initial flight depth, h1 = final flight depth, L/D chine to be offered with additional =Length/diameter ratio, h/h1 = Compression ratio

Injection molding


163 downstream end of the screw may be equipped with a valve arrangement to prevent melt flowing back down the screw flights. This is the mold filling or injection phase. After the mold is filled, screw pressure is maintained for short period to compensate for volumetric shrinkage of the cooling melt contained in the mold. This is the packing or holding phase. At the conclusion of the holding phase, and while the mold remains closed for the molding to cool to ejection temperature, the injection unit cycle recommences with the resumption of screw rotation and melt preparation. Injection units are rated in terms of the maximum injection pressure and injection volume available. Injection pressure is the theoretical maximum available at the downstream end of the screw. This is a function of the screw diameter and the force acting on it. It should not be confused, as it often is, with the hydraulic line pressure acting on the injec-

Preferred screws for use with polypropylene should have an L/D ratio in the range 20:1 to 25:1, and a compression ratio of 2.3:1 to 2.8:1. The basic sequence of events in the injection unit is: The screw rotates, so heating and melting the material which is conveyed along the screw flights to the downstream end of the screw. The barrel nozzle is closed by thermal or mechanical valve means or by the presence of a previouslymade molding. The accumulating melt presses the still-rotating screw back against a controlled resistance (the back pressure) until sufficient melt has accumulated to make the next molding. At this point, screw rotation stops. This is the melt preparation phase. The barrel nozzle is opened and the screw performs the action of a ram by moving forward in the axial direction without rotating. This forces (injects) the melt that has accumulated ahead of the downstream end of the screw through the nozzle and into the mold. The Table 14.2 Injection pressure conversion table Nominal value (psi)

Equiv. Value (bar)

Equiv. Value (MPa)

Nominal value (bar)

Equiv. Value (psi)

Equiv. Value (MPa)

Nominal value (MPa)

Equiv. Value (psi)

Equiv. Value (bar)

10000

689.5

68.9

600

8702.3

60.0

60

8702.3

600.0

11000

758.4

75.8

700

10152.7

70.0

70

10152.7

700.0

12000

827.4

82.7

800

11603.0

80.0

80

11603.0

800.0

13000

896.3

89.6

900

13053.4

90.0

90

13053.4

900.0

14000

965.3

96.5

950

13778.6

95.0

95

13778.6

950.0

15000

1034.2

103.4

1000

14503.8

100.0

100

14503.8

1000.0

16000

1103.2

110.3

1050

15229.0

105.0

105

15229.0

1050.0

17000

1172.1

117.2

1100

15954.2

110.0

110

15954.2

1100.0

18000

1241.1

124.1

1150

16679.4

115.0

115

16679.4

1150.0

19000

1310.0

131.0

1200

17404.6

120.0

120

17404.6

1200.0

20000

1379.0

137.9

1250

18129.8

125.0

125

18129.8

1250.0

21000

1447.9

144.8

1300

18854.9

130.0

130

18854.9

1300.0

22000

1516.8

151.7

1350

19580.1

135.0

135

19580.1

1350.0

23000

1585.8

158.6

1400

20305.3

140.0

140

20305.3

1400.0

24000

1654.7

165.5

1450

21030.5

145.0

145

21030.5

1450.0

25000

1723.7

172.4

1500

21755.7

150.0

150

21755.7

1500.0

26000

1792.6

179.3

1600

23206.1

160.0

160

23206.1

1600.0

27000

1861.6

186.2

1700

24656.5

170.0

170

24656.5

1700.0

28000

1930.5

193.1

1800

26106.8

180.0

180

26106.8

1800.0

29000

1999.5

199.9

1900

27557.2

190.0

190

27557.2

1900.0

30000

2068.4

206.8

2000

29007.6

200.0

200

29007.6

2000.0


Injection molding

164 tion cylinder that supplies the force to the screw. Nor should it be taken as the pressure available to fill the mold cavities. This is much less because of pressure losses in the nozzle and mold feed systems. Injection pressures are normally quoted in megaPascals (MPa), atmospheric pressures (bar), or pounds per square inch (psi) (Table 14.2). The maximum injection volume or swept volume is the product of the screw diameter and its maximum retraction stroke during plasticizing. The 3 value is expressed in cubic centimeters (cm ), cubic 3 inches (in ), and sometimes as the weight in ounces (oz) or grams (gm) of plastic material that can be injected (Table 14.3). The weight rating is a less accurate measure and is relative to the density of the plastics material in question. Quoted injection weight or shot weight ratings are usually referenced

to GP polystyrene. The figure used to make the conversion should be the density in the melt state rather than in the solid state (Table 14.4). In principle, the entire theoretical shot volume is available for injection. In practice, the volume is limited by the concept of residence time. This is the time that an element of plastics material takes to pass through the screw and barrel system. It is a function of cycle time and injection stroke. The significance of residence time rests on the fact that a plastics material may begin to degrade if exposed too long to process temperatures normally regarded as safe. Residence time itself is independent of material, but the sensitivity of materials to residence time varies and is at its greatest with materials such as PVC that are processed at a point close to the degradation temperature. Polypropyl-

Table 14.3 Shot volume conversion table Nominal shot volume (cm3)

Equiv. Volume (in3)

Equiv. shot weight in GPPS (gm)

Equiv. Shot weight in GPPS (oz)

Nominal shot volume (in3)

Equiv. Volume (cm3)

Equiv. Shot weight in GPPS (gm)

Equiv shot weight in GPPS (oz)

25

1.5

22.0

0.8

2

32.8

28.8

1.0

50

3.1

44.0

1.6

3

49.2

43.3

1.5

75

4.6

66.0

2.3

4

65.5

57.7

2.0

100

6.1

88.0

3.1

5

81.9

72.1

2.5

125

7.6

110.0

3.9

6

98.3

86.5

3.1

150

9.2

132.0

4.7

7

114.7

100.9

3.6

175

10.7

154.0

5.4

8

131.1

115.4

4.1

200

12.2

176.0

6.2

9

147.5

129.8

4.6

250

15.3

220.0

7.8

10

163.9

144.2

5.1

300

18.3

264.0

9.3

20

327.7

288.4

10.2

350

21.4

308.0

10.9

30

491.6

432.6

15.3

400

24.4

352.0

12.4

40

655.5

576.8

20.3

450

27.5

396.0

14.0

50

819.4

721.0

25.4

500

30.5

440.0

15.5

60

983.2

865.2

30.5

750

45.8

660.0

23.3

70

1147.1

1009.4

35.6

1000

61.0

880.0

31.0

80

1311.0

1153.6

40.7

1500

91.5

1320.0

46.6

90

1474.8

1297.9

45.8

2000

122.0

1760.0

62.1

100

1638.7

1442.1

50.9

2500

152.6

2200.0

77.6

150

2458.1

2163.1

76.3

3000

183.1

2640.0

93.1

200

3277.4

2884.1

101.7

4000

244.1

3520.0

124.2

250

4096.8

3605.2

127.2

5000

305.1

4400.0

155.2

500

8193.5

7210.3

254.3

10000

610.2

8800.0

310.4

750

12290.3

10815.5

381.5

15000

915.4

13200.0

465.6

1000

16387.1

14420.6

508.7

Injection molding


165 Table 14.4 Shot weight conversion factors Multiply volume (cm3) by this factor to obtain shot weight (gm)

Multiply volume (cm3) by this factor to obtain shot weight (oz)

Multiply volume (in3) by this factor to obtain shot weight (gm)

Multiply volume (in3) by this factor to obtain shot weight (oz)

LD polyethylene

0.79

0.028

12.95

0.46

HD polyethylene

0.81

0.029

13.27

0.47

Polypropylene

0.85

0.030

13.93

0.49

Polystyrene

0.88

0.031

14.42

0.51

ABS

0.89

0.031

14.58

0.51

PPO

0.92

0.032

15.08

0.53

SAN

0.92

0.032

15.08

0.53

Polyamide 6/6

0.95

0.034

15.57

0.55

Polyamide 6/6

0.97

0.034

15.90

0.56

PMMA

1.01

0.036

16.55

0.58

Polycarbonate

1.01

0.036

16.55

0.58

PBT

1.12

0.040

18.35

0.65

PET

1.15

0.041

18.85

0.66

PVC-U

1.15

0.041

18.85

0.66

Acetal

1.22

0.043

19.99

0.71

PES

1.48

0.052

24.25

0.86

Polymer

ene has a tendency to oxidize and is routinely protected by the inclusion of anti-oxidants in the polymer production process. It is consequently unwise to expose polypropylene to lengthy residence times in the injection unit. Small shots produced from big machines are likely to lead to trouble, especially if the cycle time is slow. The chart (Figure 14.7) shows residence times for a range of cycle times. Injection strokes are expressed in terms of D, the screw diameter. If for example, we wish to limit residence time to 5 minutes, this means that the injection stroke should not be less than about 1D for a 50 second cycle, or not less than about 0.6D for a 30 second cycle. The maximum injection stroke for a typical injection molding screw is about 4D, so the two figures equate to about 25% and 15% of maximum shot volume respectively. The preferred shot volume is in the range 1D to 3D, or 25% to 75% of the maximum available. Allowable residence times for polypropylene depend on the material temperature. At 280°C, observable degradation occurs at about five minutes exposure. At 250°C the material will tolerate a much longer exposure. The European Committee of Machinery Manufacturers for the Plastics & Rubber Industries has


developed a standard classification for injection molding machines. This is known as the Euromap international size classification and it consists of two numbers in the format xxx/xxx. The first number indicates the clamp force in kiloNewtons (kN). The second number is an injection unit rating derived by multiplying the maximum injection pressure (bar) by the shot volume (cm3) and dividing by 1000. This figure is useful for classifying injection molding machines that are supplied, as most are, with a choice of screw diameters. The maximum injection force exerted by the machine on the screw remains constant because only the screw and barrel assembly is interchanged. This means that shot volume is proportional to screw diameter but the maximum injection pressure is inversely proportional. The Euromap injection unit rating is unaffected by screw diameter. In other words, it returns the same figure for each of the alternative screw and barrel assemblies for a particular machine and so simplifies the task of classification. This rating is not much help in specifying an injection molding machine; maximum shot volume and injection pressure figures are indispensable for that purpose. The normal screw and barrel assembly is designed for a maximum injection pressure in the region of 1500 bar (21,800 psi). A low-pressure high-

Injection molding

166

18

16

14

Residence time (minutes)

12

10 sec cycle 20 sec cycle 30 sec cycle 40 sec cycle 50 sec cycle 60 sec cycle 90 sec cycle

10

8

6

4

2

0 0.5

1

1.5

2

2.5

3

Injection stroke (D)

Figure 14.7 Material residence times. [1175]

volume alternative will operate in the region of 1200 bar (17,400 psi), while the high-pressure lowvolume version will work at about 2000 bar (29,000 psi). Once again, these are the theoretical maxima at the downstream face of the screw. Thereafter, major pressure losses occur in forcing the plastics melt through the injection nozzle and thence through the mold feed system and cavities. These pressure losses cannot be quantified by simple rules. They are a function of the physical form of the flow path, the condition of the plastics melt, the rate of heat

Figure 14.8 Example of computer-predicted pressure drops for a balanced 8-cavity mold using Profax SB–823 polypropylene. [1175]

Injection molding

exchange, the type of polymer, and the rate and pressure of injection. Specific figures can be calculated with adequate accuracy by computer simulations of the molding process. The example (Figure 14.8) shown holds good only for a specific combination of mold, material, machine, and process conditions, but it serves to illustrate the way in which theoretical maximum injection pressure is diminished before reaching the cavity. Pressure losses in the machine nozzle may account for a further cut of 200 psi to 1000 psi. 14.2.3 Power systems Injection molding machines perform a wide range of mechanical movements with differing characteristics. Mold opening is a low-force highspeed movement, and mold closing a high-force low-speed movement. Plasticizing involves high torque and low rotational speed, while injection requires high force and medium speed. A source of motive power is needed to drive these movements. The modern injection molding machine is virtually always a self-contained unit incorporat-


167

gate freezes

ing its own power source. Early maCycle complete cycle chine frequency ran from a centralized source serving an entire shop or factory. Clamp closed open In this respect, injection molding machines have undergone the same metaPhases injection cooling ejection morphosis as machine tools. Oil hydraulics has become firmly Screw inject hold plasticize established as the drive system for the vast majority of injection molding machines and until recently was almost unShrinkage part shrinks in mold challenged as the power source. Put at its simplest, the injection molding maCooling part cools in mold chine contains a reservoir of hydraulic oil which is pumped by an electricallyFigure 14.9 Principal elements of the injection molding cycle driven pump at high pressure, typically at up to 2000 psi, to actuating cylinders peatability than hydraulic systems. and motors. High and low pressure linear movements are performed by hydraulic cylinders, and 14.2.4 Control systems rotary movements for screw drive and other purThe full sequence of operations and necessary opposes are achieved by hydraulic motors. Hybrid tions in a modern injection molding machine is very machines, in which the screw is driven by electric complex (Figure 14.9). So too, is the range of pamotor while the linear movements remain hydraurameters and adjustments needed to control the prolically powered, are not uncommon. cess accurately and automatically (Table 14.5). In recent years, the supremacy of the hydraulic Control is ultimately exercised by valves, regulators machine has been challenged by all-electric maand switches but it is rare now for these to be under chines. These use new brushless servo motor techindividual manual control. The norm now is elecnology to power the various machine movements. tronic control of varying degrees of sophistication The capital cost of all-electric machines is higher ranging from simple partial control by programmathan that of conventional machines but the energy ble logic controller up to full centralized computer consumption in production is much lower. This is control. It is usual for an injection molding machine because the electric motors run only on demand, to be offered with a choice of control options to suit and there are no losses due to energy conversion, a variety of end uses and budgets. pipelines, or throttling. The elimination of hyThe precision and repeatability of injection draulic oil makes the all-electric machine inhermolding machines has been much improved by the ently cleaner, so these machines are attractive for introduction of closed loop control to critical feasterile or clean room use. There is also evidence tures like the injection screw sequence. The closed that all-electric machine movements can be reloop principle uses sensors to measure an imporsolved with a higher degree of precision and reTable 14.5 Some injection molding process control factors Temperature

Time

Distance

Speed

Pressure or force Profile

Melt

Hold changeover

Hold changeover

Screw rotation

Hold changeover

Injection pressure

Mold

Open

Fast open

Injection stroke

Injection

Injection speed

Nozzle

Carriage forward delay

Slow open

Carriage

Peak

Holding pressure

Barrel zones

Hold

Eject

Slow break

Holding

Feed throat

Carriage back delay

Sprue break

Fast open

Back

Screw start delay

Suck back

Slow open

Nozzle hold-on

Cooling

Shot

Eject

Clamp close

Eject

Cushion

Pellets

Clamp open

Cycle delay


Injection molding

168 tant parameter — speed, position, pressure — of the element to be controlled. The readings are processed by the control system which generates control signals to a servo valve that regulates the element. The process is often known as feedback. In effect, the system monitors itself to check whether it is performing as instructed and if not, it makes an adjustment based on the discrepancy.

14.3 Process conditions for polypropylene Process conditions vary significantly from one molding project to another, depending not only on the configuration of the part but also on mold design, machine choice, and on the desired balance of properties and attributes in the finished part. Consequently, these process recommendations for polypropylene can be regarded as guidelines only. However, they will serve as a reliable starting point for the optimization of the injection molding process. 14.3.1 Filling Like other thermoplastics, polypropylene can be

injection molded over a range of melt and mold temperatures. The table (Table 14.6) sets out the extremes that are practicable. In reality, most processing is performed in a narrower mid-range of values while the extremes are reserved for special circumstances. Polypropylene melt temperatures will normally be in the range 230°C to 260°C and mold temperatures in the region of 20°C to 40°C. Lower mold temperatures produced with a mold chiller may be used for fast-cycling parts with a high injection rate. A warmer mold improves surface gloss and weld lines. Mold temperatures above 60°C may be necessary when producing thick-walled parts; otherwise, premature surface freezing may result in the formation of internal voids. The desired melt temperature is attained by gradually raising the temperature of the material as it travels along the screw. Heat is gained by conduction from the heated barrel and by shear work done on the material. It is usual to set the barrel heating zones in a gradually increasing temperature profile (Figure 14.10). There are normally more than three zones of temperature control on the barrel. The table (Table

Table 14.6 Melt and mold temperature ranges for polypropylene compared with other thermoplastics. Melt temperature (°C )

Melt temperature (°F )

Mold temperature (°C )

Mold temperature (°F )

Polypropylene

200–300

390–570

20–90

70–195

ABS

200 –260

390–500

50–80

120–175

Acetal

180–320

355–445

60–120

140–250

HD polyethylene

200–300

390–570

10–60

50–140

LD polyethylene

160–270

320–520

20–60

70–140

PBT

230–280

445–535

40–80

105–175

PES

320–380

610–715

90–160

195–320

PET

260–300

500–570

130–150

265–300

PMMA

190–290

375–555

40–90

105–195

Polyamide 11

200–270

390–520

40–80

105–175

Polyamide 12

190–270

375–520

20–100

70–210

Polyamide 6

240–290

465–555

40–120

105–250

Polyamide 6/10

230–290

445–555

40–120

105–250

Polyamide 6/6

260–300

500–570

40–120

105 –250

Polycarbonate

270–380

520–715

80–120

175–250

Polystyrene

170–280

340–535

10–60

50–140

PPO

250–300

480–570

30–110

85–300

PVC-U

170–210

340–410

20–60

70–140

SAN

200–260

390–500

50–80

120–175

Polymer

Injection molding


169

Figure 14.10 Temperature profile for DSM Stamytec high crystallinity polypropylene.

14.7) shows a typical range of barrel temperature settings for polypropylene. The shot volume can be up to 85% of the machine maximum shot volume. The minimum shot volume is determined by residence time in the way discussed earlier. If the injection proportion is being judged in terms of shot weight, remember to multiply the machine rating by a factor of 0.85 to convert it from the polystyrene standard to polypropylene. Relatively high injection pressures are used, typically in the range 1200 bar (17,400 psi) to 1800 bar (26,100 psi). Hold pressure can be 40% to 80% of injection pressure, and hold times are relatively long to avoid sinks and to compensate for the high volume reduction when a semi-crystalline material passes from the melt state to the solid state. As is normal in injection molding, the screw should not be allowed to bottom at the forward limit of the injection stroke. The amount of melt remaining ahead of the screw in this condition is known as the cushion; for polypropylene this should be in the range 2 mm (0.079 in) to 6 mm (0.24 in) thick. Back pres-

sure during screw rotation can be in the range 100 bar (1450 psi) to 300 bar (4400 psi). Higher values result in better mixing of masterbatch or other additives, but will require the use of a valved nozzle to prevent drooling. The principal parameters affecting the flow of plastics melt during injection are injection rate and melt temperature. Injection rate is directly controlled in closed-loop injection systems; the injection pressure in the filling phase is whatever is needed to generate the chosen rate. In open-loop systems, the pressure is chosen and the injection rate is uncontrolled. The viscosity of a plastics melt varies with shear rate and temperature, and shear rate is proportional to injection rate, so an uncontrolled injection rate is less than ideal. In other words, closed loop injection systems should be the norm for consistent results. The difficulty faced by those optimizing an injection molding project is to know whether it is more productive to improve melt flow by raising the melt temperature or increasing the injection rate (shear rate). The answer depends on the characteristics of the material. The viscosity of a polypropylene melt is sensitive to shear rate but the extent of this sensitivity depends on the molecular weight distribution of the particular grade. Those with a wide molecular weight distribution respond the most to an increase in shear rate. For polypropylene materials as a class, it will be more effective to deal with mold

Table 14.7 Typical barrel zone temperature settings for polypropylene.

Zone

Temperature setting Temperature setting (°C ) (°F )

1

150–210

300–410

2

210–250

410–480

3

220–250

430–480

4

220–250

430–480

Figure 14.11 Flow path length as a function of melt

Nozzle

240–260

465–500

temperature for various grades of Hoechst Hostalen polypropylene.


Injection molding

170

Figure 14.12 2mm thick flow path length as a function of specific injection pressure for various grades of Hoechst Hostalen polypropylene.

filling problems by increasing the injection rate rather than raising the melt temperature. Raising the mold temperature may appear to be an alternative strategy, but this has very little effect on flow provided injection rates are rapid enough to prevent the premature freezing of thin sections. A practical measure of polypropylene flow under injection molding conditions is the flow path length. The graphs demonstrate the effects of melt temperature (Figure 14.11), injection pressure (Figure 14.12), and fillers and reinforcements (Figure 14.13, Figure 14.14) on the maximum flow path length obtainable with various grades of polypropylene. 14.3.2 Clamp The clamp force requirement for a polypropylene injection molding is best established by the use of a computer flow simulation that will determine the pressure gradients throughout the cavities and feed system and will reflect the effect on pressure of the material characteristics and the many process parameters. The comparative accuracy of the figure means that only a small safety margin need be applied, and this in turn ensures that the injection molding machine selected is the smallest possible. Since hourly running costs are related to machine size, the effect is to minimize the production cost of the molding, and so it is worth paying attention to clamp force determination.

Injection molding

Figure 14.13 Flow path length as a function of wall thickness for various reinforced grades of Hoechst Hostacom polypropylene Conditions: melt 250°C, mold 60°C, injection pressure 750 bar, injection rate 60% of maximum. Key: a = Hostacom M2 N02 20% talc filler, improved impact strength, b = Hostacom M2 N01 20% talc filler, c = Hostacom G2 N02 20% coupled glass fiber reinforcement, d = Hostacom G2 N03 20% glass microspheres, e = Hostacom M4 N01 40% talc filler, f = Hostacom G2 N01 20% glass fiber reinforcement, g = Hostacom G3 N01 30% coupled glass fiber reinforcement, h = Hostacom M1 U01 10% talc filler, i = Hostacom M4 U01 40% talc filler, improved flow .

Underestimation of the force requirement may lead to the choice of a machine with insufficient clamp force. If so, the mold will open slightly during injection, causing an overflow or flash as it is known, to be formed on the molding. The remedy is to use a machine with a greater clamp force, at a consequential cost disadvantage. If a computer simulation is not available, the chart (Figure 14.15) and table (Table 14.8) can be used to calculate the required clamp force but the margin of uncertainty will be greater and the use of a larger safety factor of some 25% to 50% is advisable. To calculate clamp force: Find the longest flow path in the molding and divide it by the wall thickness. This gives the ratio of flow path length to thickness. Find the corresponding curve on the chart. If the ratio is not an exact match, either choose the next highest curve or interpolate a curve.


171 Table 14.8 Material factors for clamp force determination. Polymer

Material factor

LD polyethylene

1

Polystyrene

1

Polypropylene

1.0–1.2

HD polyethylene

1.0–1.3

Polyamide 11

1.2–1.4

Polyamide 12

1.2–1.4

Polyamide 6

1.2–1.4

Polyamide 6/10

1.2–1.4

Polyamide 6/6

1.2–1.4

ABS

1.3–1.5

PMMA

1.5–1.7

Polycarbonate

1.7–2

PVC-U

Figure 14.14 Flow path length as a function of wall thickness and injection pressure for talc filled grades of Hoechst Hostacom polypropylene. Conditions: melt 230°C, mold 60°C, injection rate 60% of maximum. Key: a = Hoechst Hostacom M1 U01 10% talc filler, b = Hoechst Hostacom M4 U01 40% talc filler, improved flow.

Trace a vertical line from the wall thickness (mm) to the chosen curve. Where this cuts the curve, trace a horizontal line to the pressure axis and read off the cavity pressure (bar). Calculate the notional clamp force (kN) by multiplying cavity pressure (bar) by the mold projected area (cm2) and dividing by 100. Adjust the clamp force by multiplying the notional figure by the appropriate material factor from the table. The resulting force figure represents a molding of simple configuration. Moldings with complex flow paths and varying thicknesses will require a higher clamp force. 14.3.3 Shrinkage and warping Polypropylene injection moldings shrink on and after removal from the mold. The magnitude of shrinkage ranges from 1.2% to 2.5%. To create the right dimensions in the molded part, the dimensions of the mold cavity must by increased by an amount known as the shrinkage allowance. Shrinkage is not only a matter of thermal expan-


2

sion and contraction but must also take account of the fact that the injected melt is compressible at injection pressures. These pressures vary throughout the molded part and therefore so too does shrinkage. For semi-crystalline materials such as polypropylene, the effect is exaggerated by a sharp change in specific volume associated with crystalline fusion. There is also a directional aspect to polypropylene shrinkage. The material shrinks more in the direction of flow than in the transverse direction. This is known as anisotropic shrinkage and is a consequence of the long-chain molecular structure which leads to a partial orientation and stretching of the chains during melt flow. The effect is more marked

Figure 14.15 Chart for determination of clamp force.

Injection molding

172 Table 14.9 Some factors influencing polypropylene shrinkage. Parameter

Increase

Maximum shrinkage variation (%) Notes

Mold temperature

20°C to 90°C

+ 0.6

Wall thickness

1mm to 6mm

+ 0.5

Duration of holding pressure

up to 20 sec

- 0.3

min. wall thickness 2mm

600 bar to 1400 bar

- 0.3

min. wall thickness 2mm

220°C to 280°C

+ 0.3

1 g/10 min to 50 g/10 min

- 0.3

Magnitude of injection/holding pressure Melt temperature Melt flow rate

in polypropylenes with a wide molecular weight distribution and is at its least in grades that have a narrow distribution of molecular weight. The range of difference between the two shrinkage values in conventional grades of polypropylene is of the order of 0.1% to 0.5%. For controlled rheology grades the differential is much less, perhaps 0.03% to 0.05%. This is due to the particularly narrow molecular weight distribution of these grades. Differential shrinkage results in a distorted or warped molding. The remedy is to eliminate as far as possible the conditions that cause the differentials. Wall thicknesses should be constant, cooling uniform, and the various flow paths in the mold should be designed to fill at the same time and under the same conditions of pressure and shear rate. Shrinkage is not an instantaneous effect. The greater part of shrinkage will be evident immediately on removal from the mold but further changes take place at a rapidly decelerating rate as the part cools completely throughout its thickness. During this time, crystallization and relaxation of internal stresses both continue slowly. The phenomenon is known as post shrinkage and may amount to about 1%. Consequently, measurements of critical dimensions should not be made sooner than 24 hours after molding. Changes may continue after 24 hours but the rate of change will be very slow at normal room temperatures. As shrinkage is a function of temperature, pressure and shear rate, the injection molding conditions will also have a significant effect on the final dimensions of the part. Taken in combination, these considerations make it impossible to quote the molder or mold designer a single simple and precise shrinkage factor (Table 14.9, Figure 14.16). That in turn means it is difficult to injection mold polypropylene to precision tolerances.

The presence of fillers and reinforcements affects the shrinkage of polypropylene in different ways, depending on the nature of the additive. Particulate fillers such as talc or glass beads reduce the shrinkage to a value in the range 0.5% to 1.6%. The shrinkage differential is also reduced from near zero to about 0.15%, so these materials have less tendency to warp than unfilled polypropylenes. Fibrous reinforcements such as glass also reduce the overall value of shrinkage but increase the differential shrinkage, and so increase the tendency to warp. The shrinkage of conventional glass grades is roughly 0.7% to 1.8% but that of coupled glass grades is much lower at about 0.4% to 1.2%. The effect is due to the very strong bond between coupled glass fibers and the polypropylene matrix. The increase in differential shrinkage is due to the tendency of the fibers to become partially oriented in the flow direction. This means that the fibers exert a much greater resistance to shrinkage in the flow direction than in the transverse direction. The differential for conventional glass fiber grades is about 0.3% to 0.5% but is much worse for coupled glass grades, rising to about 0.8%.

Figure 14.16 Shrinkage as a function of part thickness and gate area.

Injection molding


173 Post shrinkage of reinforced and filled polypropylenes is limited to about 0.5% or less. 14.3.4 Injection molding long-fiber reinforced grades Experience has shown that polypropylene grades reinforced with long glass fibers (10 mm to 12 mm long) do not suffer as much fiber damage during injection molding as was first expected. Some degree of fiber damage is acceptable, provided the aspect ratio remains above a critical value. So to preserve the benefits of long-fiber reinforcement, the molding conditions should be chosen to minimize fiber fracture. During plasticizing, the melt shear stress should be held as low as possible by using a low screw speed with a high melt temperature. The screw should be fitted with a ring non-return valve rather than the ball type. Nozzles, runners and gates should be large to minimize shear. A direct sprue gate is ideal. Screw and mold wear is, if anything, less than that experienced with shortfiber glass reinforced materials. This is due to the relatively small number of fiber ends present in long-fiber grades.

14.3.5 Injection molding metallocene grades Metallocene grades of polypropylene are very new and are not yet extensively used in injection molding, so process guidelines are slow to emerge. The first indications are that high injection speeds and packing pressures should be used. Back pressure should be as low as possible. Barrel temperatures should be substantially uniform, apart from the feed zone. The temperature range is 175°C to 290°C. Mold temperatures should be as low as possible with 10°C as a suggested ideal. 14.3.6 Troubleshooting The complexity of the injection molding process, and the inter-dependence of the many variables involved, means that any molding defect may have several different causes, of which more than one may be present at any given time. Consequently a remedy that cures one fault may engender another. Attempts to describe cause and effect in terms of computer expert systems have so far met with at best very limited success. The conclusion is that injection molding troubleshooting is a job for the expert. Provided these limitations are understood, the trouble shooting chart (Table 14.10) will provide a useful guide for problem solving.

Table 14.10 Injection molding trouble shooting chart. [1049] Problem

Short shots

Possible cause

Suggested remedy

Insufficient feed

Increase

Insufficient pressure

Increase

Melt temperature too low

Lengthen cycle Increase temperature gradually Increase screw speed and back pressure

Injection time too short

Increase

Nozzle cold on start-up

Fit nozzle heater

Mold too cold

Reduce coolant flow Fit mold temperature controller

Feed system too small

Enlarge sprue or runner or gate

Air trapped in mold

Add or clean vents

Plasticizing capacity inadequate.

Increase cycle time Use a larger machine

Unbalanced cavity in multi-cavity mold

Adjust runner or gate size

Excessively thin region

Redesign part


Injection molding

174 Table 14.10 Injection molding troubleshooting chart. [1049] (continued) Problem

Possible cause

Suggested remedy

Melt temperature too high

Reduce barrel temperatures

Insufficient material injected

Increase feed Raise barrel temperatures Increase mold temperature Enlarge gates

Insufficient dwell time

Increase

Premature gate freezing

Enlarge gate Increase mold temperature

Sharp variations in wall thickness

Redesign part

Wrong gate location

Relocate

Part ejected too hot

Increase cooling time Use nucleated grade

Cavity pressure too low

Increase Raise barrel temperatures Increase mold temperature Enlarge gate

Volatiles from overheated material

Reduce heating

Condensation on granules

Pre-dry Improve storage

Premature freezing of flow path to thick section

Increase pressure Increase mold temperature Use nucleated grade Enlarge gates

Mold too cold

Increase mold temperature Increase pressure Increase injection speed

Mold too hot

Cool mold near gate

Excessive injection pressure

Reduce pressure Reduce runners

Excessive melt temperature

Reduce heating

Mold parting face faulty

Repair mold

Insufficient clamp force

Increase Use a larger machine

Foreign matter on mold parting face

Clean mold

Flow restriction in one or more cavities of multi-cavity mold

Identify and remove

Flow marks


Increase heating

Weld lines

Incorrect gate location

Relocate

Incorrect gate type

Adjust

Injection pressure too low

Increase

Inadequate venting

Vent cavity

Mold cavity soiled

Clean mold

Mold temperature too low

Increase

Flow length too great

Relocate gate Increase number of gates

Excessive use of mold lubricant

Mold lubricant not recommended

Sink marks

Voids

Surface defects near gate

Flash

Bad surface finish

Injection molding


175 Table 14.10 Injection molding trouble shooting chart. [1049] (continued) Problem

Brittleness

Warping

Silver streaks

Nozzle drool

Burn marks

Parts sticking

Possible cause

Suggested remedy


Increase heating

Mold too cold

Increase mold temperature

Melt degraded by excessive heating

Decrease heating

Material contaminated

Clean hopper and barrel

Incorrect part design

Redesign part

Excessive use of regrind

Reduce proportion of regrind


Increase heating

Incorrect part design

Redesign part

Overpacking near gate

Reduce shot volume Reduce injection pressure Reduce injection time Reduce heating Check runner and gate sizes

Sharp variations in wall thickness

Redesign part

Flow length too great

Relocate gate Increase number of gates

Unbalanced multiple gates

Relocate gates Balance feed system

Part ejected too hot

Increase cooling time Use nucleated grade

Inadequate or badly located ejectors

Modify mold

Temperature variations between the mold halves

Adjust cooling circuits Modify mold


Increase heating

Mold too cold

Increase mold temperature

Condensation on mold

Dry mold Increase mold temperature

Entrapped volatiles

Pre-dry material Improve storage Vent mold

Excessive nozzle temperature

Reduce heating

Excessive melt temperature

Reduce heating Purge barrel

Incorrect filling pattern

Relocate gate Improve venting

Molding too hot

Increase cooling

Insufficient draft on side walls

Increase draft angle

Excessive injection pressure

Decrease

Cavity finish poor

Polish mold

Cores misaligned by injection pressure

Redesign part Relocate gate


Injection molding

176

14.4 Injection molds 14.4.1 Introduction The injection mold performs two vital functions. It defines the shape of the molded part, and it acts as a heat exchanger to cool the plastics material from melt temperature to ejection temperature. It must be very robustly engineered to withstand injection and clamping forces, it must operate automatically at high speed, and it must be built to very high standards of precision and finish. The mold also has

other less obvious influences on the finished part. The dimensions and properties of the molding are greatly affected by shear rates, shear stresses, flow patterns, and cooling rates. Some of these are affected by both mold and machine; others are almost exclusively a function of the mold. These factors combine to make the injection mold a costly item. Modern technologies in the form of concurrent engineering, computer-aided analysis of flow and cooling, high-speed and computer-controlled machining can help to keep the cost 1. 2. 3. 4. 5. 6. 7. 8. 9. 10. 11. 12. 13. 14. 15. 16. 17. 18. 19.

Figure 14.17 Example of injection mold illustrating principal component parts. [1196]


20. 21. 22. 23. 24. 25. 26. 27. 28. 29. 30. 31. 32. 33. 34. 35. 36. 37. 38. 39. 40. 41. 42. 43. 44. 45. 46. 47. 48. 49. 50. 51. 52.

Back plate Back plate Cavity holder plate Core holder plate Support plate Riser block Ejector plate Ejector back plate Locating ring Locating ring Locating guide pillar Stripper rod Ejector coupling rod Locating guide bush Heated nozzle Stripper rod guide bush Ejector bush Thermal insulating plate Electrical service connector box for heated nozzle Centering sleeve Alignment dowel Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Cap screw Ejector coupling rod connector Ball catch Ejector pin Ejector stop button Support pillar Spring washer Spring washer O-ring seal Water channel service coupling Water channel sealing plug Cooling water spiral core O-ring seal O-ring seal Pressure sensor Core insert block Cavity insert block Stripper bar Side action Cam Cap screw

Injection molding

177 down. So too can the use of standard mold components that enjoy economies of scale and specialization. Even so, mold costs frequently dismay purchasers of moldings and there can be pressure to cut costs by reducing mold quality. This is a false economy and will almost always result in a more expensive molding. There is no substitute for a quality mold. 14.4.2 Injection Mold Components The figure (Figure 14.17) illustrates the principal components used in the construction of an injection mold. The sequence of operations (Figure 14.18) for a typical mold is: Plastics material is injected into the closed mold. The mold remains closed while the molding cools. The mold temperature is controlled by a coolant fluid (generally water or oil) which is pumped through cooling channels. Even if the mold is heated relative to ambient temperature it is still cool in relation to the plastics melt temperature. The mold opens, leaving the molding attached by shrinkage to the core. During opening the side action is retracted by a cam to release an undercut on the molding. The ejector plate is moved forward, causing ejector pins and stripper bars to push the molding off the core. The ejector plate returns and the mold closes, ready for the next cycle.

14.4.3 Injection Mold Types Every molded part is different and so every mold is a one-off. Nevertheless, it is possible to distinguish some standard features and types. All are suitable for use with polypropylene. The principal types are two-plate, three-plate, and stack molds. A further distinction concerns the feed system which can be either the cold or hot type. These classifications overlap. A three-plate mold will have a cold runner feed system, and a stack mold will have a hot runner system. Two plate molds can have either feed system. 14.4.3.1 2-plate The two-plate mold has more than two plates in its construction. The description means that the mold opens or splits into two principal parts (Figure 14.19). These are known as the fixed or injection half which is attached to the machine fixed platen, and the moving or ejection half which is attached to the moving platen. This is the simplest type of injection mold and can be adapted to almost any type of molding. The cavities and cores that define the shape of the molding — these are sometimes known as the impressions — are so arranged that when the mold opens, the molding remains on the ejection half of the mold. In the simplest case, this is determined by shrinkage that causes the molding to grip on the core. Sometimes it may be necessary to adopt positive measures such as undercut features or cavity air blast to ensure that the molding remains in the ejection half of the mold.

Figure 14.18 Sequence of mold operations.


Injection molding

178

Figure 14.19 Schematic of 2-plate mold. A-Knockout plate, B-Ejector retainer plate, C-Ejector travel, D-Support plate, E-Sleeve-type ejector, F-Rear cavity plate, G-Cavity, H-Front cavity plate, I-Locating ring, J-Sprue bushing, K-Clamping plate, L-Parting line, M-Core or force, N-Ejector pin, O-Sprue puller, P-Clamping plate, Q-Retainer plate, R-Knockout pins, S-Core or force pin.

14.4.3.2 3-plate The 3-plate mold is so called because it splits into three principal linked parts when the machine clamp opens (Figure 14.20). As well as the fixed and moving parts equating to the 2-plate mold there is an intermediate floating cavity plate. The feed system is housed between the fixed injection half and

Figure 14.20 Schematic of 3-plate gate.

Injection molding

the floating cavity plate. When the mold opens it is extracted from the first daylight formed by these plates parting. The cavity and core is housed between the other side of the floating cavity plate and the moving ejection part of the mold. Moldings are extracted from the second daylight when these plates part. The mold needs separate ejection systems for the feed system and the moldings. Motive power for the feed system ejector and the movement of the floating cavity plate is derived from the clamp opening stroke by a variety of linkage devices. The molding ejection system is powered normally by the injection machine ejection system. The 3-plate mold is normally used when it is necessary to inject multiple cavities in central rather than edge positions. This is done for flow reasons, to avoid gas traps, ovality caused by differential shrinkage, or core deflection caused by unbalanced flow. This type of mold also has the advantage of automatically removing (degating) the feed system from the molding. The disadvantages are that the volume of the feed system is greater than that of a 2-plate mold for the same component, and that the mold construction is more complicated and costly. 14.4.3.3 Stack The stack mold also features two or more daylights in the open position. Two daylights is the normal form (Figure 14.21) but up to four are known. The purpose of the stack mold is to increase the number of cavities in the mold without increasing the projected area and hence the clamp force required from the injection molding machine. This is done by providing cavities and cores between each of the daylights. Provided the projected area at each daylight is the same, opposed components of opening thrust from each daylight cancel out, leaving the total mold opening force no

Figure 14.21 Schematic of stack mold.


179 greater than that developed in a single daylight. The cavities are fed by a hot runner system deployed in the floating cavity plate. Separate ejection systems are required for each daylight. The mold engineering and hot runner control systems are complicated and become much more so when there are more than two daylights present. Stack molds are normally used for high volume production of relatively small and shallow components such as closures for packaging applications. 14.4.4 Injection Mold Feed system The feed system is the name given to the flow melt passage in the mold, between the nozzle of the injection molding machine and the mold cavities. This apparently utilitarian feature has a considerable effect on both the quality and economy of the molding process. The feed system must conduct the plastics melt to the cavity at the right temperature, must not impose an excessive pressure drop or shear input, and should not result in non-uniform conditions at the cavities of multi-impression molds. The feed system is an unwanted by-product of the molding process, so a further requirement is to keep the mass of the feed system at a minimum to reduce the amount of plasics material used. This last consideration is a major point of difference between cold and hot runner systems. The cold runner feed system is maintained at the same temperature as the rest of the mold. In other words, it is cold with respect to the melt temperature. The cold runner solidifies along with the molding and is ejected with it as a waste product in every cycle. The hot runner system is maintained at melt temperature as a separate thermal system within the cool mold. Plastics material within the hot runner system remains as a melt throughout the cycle, and is eventually used on the next or subsequent cycles. Consequently, there is little or no feed system waste with a hot runner system. Effectively, a hot runner system moves the interface between the machine plasticizing system and the mold to a point at or near the cavities. In a cold runner system, the interface is at the outside surface of the mold, at a point between the machine nozzle and the sprue bush. 14.4.4.1 Cold runner Cold runner feed systems include three principal components; sprue, runner, and gate. The sprue is a tapered bore in line with the axis of the injection unit, that conducts the melt to the parting line of the mold. The runner is a channel cut in a parting


Figure 14.22 Common runner configurations. [1221]

face of the mold to conduct melt from the sprue to a point very close to the cavity. The gate is a relatively small and short channel that connects the runner to the cavity. The gate is the entry point of the melt into the molding cavity. Runners are produced in a variety of crosssectional configurations (Figure 14.22), but not all of them perform equally well. The best shape for the runner itself is a full-round section, cut in both halves of the mold. This is the most efficient form for melt flow without premature cooling. There are some instances when it is desirable to cut the runner only in one half of the mold, either to reduce the machining cost or where it is mechanically necessary over moving splits. In this case, the preferred runner sections are trapezoidal or modified trapezoidal. The half-round runner provides only a restricted flow channel combined with a large surface area for cooling and consequently is not to be recommended. The concept of the hydraulic diameter (DH) provides a quantitative means of ranking the flow resistance of the various runner configurations. Hydraulic diameter is calculated from an expression chosen to give a full-round runner a value of 1D, where D is the runner diameter: DH = 4A/P where A = cross-sectional area and P = perimeter The resulting values for equivalent hydraulic diameter (Figure 14.23) clearly demonstrate the superi-

Figure 14.23 Equivalent hydraulic diameters for common runner configurations. [1221]

Injection molding

180

Figure 14.24 Balanced and unbalanced runner

quality of the moldings. Balance in a multi-cavity mold with dissimilar cavities (known as a family mold) can be achieved by careful variation of runner diameter in order to produce equal pressure drops in each flow path. Such balancing can only be achieved efficiently by the use of computer flow simulations, and this method really should now be the norm for injection mold design. If flow simulation software is used, runner dimensions will be calculated precisely and can then optionally be adjusted to a standard cutter size. If a simulation is not available, the following guidelines (Figure 14.25) suggest suitable runner sizes for use with polypropylene. These are given as a function of wall thickness and may need to be adjusted for parts that are thicker than 4 mm or thinner than 2 mm. In any case, fine tuning may be necessary during mold trials. The easiest way to do this is to start with small runners and enlarge them if necessary.

layouts.

ority of the full-round design for runners cut in both halves of the mold and the modified trapezoidal design for runners cut in one half of the mold. Runner layouts should be designed to deliver the plastics melt at the same time and at the same temperature, pressure and velocity to each cavity of a multi-cavity mold. Such a layout is known as a balanced runner (Figure 14.24). A balanced runner will usually consume more material than an unbalanced type, but this disadvantage is outweighed by the improvement in the uniformity and

14.4.4.2 Sprue The sprue (Figure 14.26) is often the thickest part in an injection molding shot and in extreme cases may influence the cycle time. Since the sprue is a waste part, this should never be allowed to happen. The reason that it sometimes does is that there is little control over the dimensions of the sprue. The length is fixed by the thickness of the fixed mold half while the diameter is largely a function of the machine nozzle bore and the necessary release taper. Sometimes the sprue can serve a useful function as a gripping point for an automated shot han-

Figure 14.25 Suggested approximate sprue and runner sizes.

Injection molding


181

Figure 14.26 Typical cold sprue design.

dling system, but the answer in most cases is to eliminate the cold sprue by means of a heated sprue bush (Figure 14.27) that serves as a limited hot runner device. In this case, the material in the bush remains as a melt while the cold runner system is injected through a vestigial sprue. Elimination of the sprue typically saves 3 grams to 5 grams of material waste per cycle. 14.4.4.3 Gates The gate is the region of the feed system between the runner and the cavity. It is the entry point by which the plastics melt enters the cavity and is an important element of the mold. Its position and dimensions have a considerable influence on the finished molding. The position of the gate or gates directly influences flow paths in the cavity, and so has a major bearing on issues such as filling pressure, weld line quality, and gas traps. Gate positions must be judged individually for each molding case. An

Figure 14.27 Example of heated sprue bush.


experienced practitioner can usually assess the best gate position for a relatively simple part geometry but for complex parts, computer-aided flow analysis is preferred for gate positioning. Gate positions should be chosen with these general recommendations in mind: Gate near a thick section to ensure that it can be packed out Position the gate where the gate scar or witness mark will not be cosmetically objectionable Position the gate where it can be easily removed with cutting tools Position the gate for flow symmetry in symmetrical parts Gate to minimize gas traps and weld lines Gate so that unbalanced flow does not take place around cores Do not place the gate at a point where high stresses or high packing could cause problems Position the gate so that flow impinges on a mold surface rather than jets into a void Position the gate to minimize shrinkage differentials The gate is usually small in relation both to the molding and the upstream feed system. There are two principal reasons for this. The gate acts as a thermal valve that seals the filled mold cavity from the feed system. When the gate freezes, no more flow can take place. A very heavy gate would be slow to freeze and would possibly allow compressed melt to flow back out of the cavity and into the feed system, so one aim of gate design is to find a size that will remain open during the injection packing phase and freeze off immediately thereafter. The other reason for a small gate is so that the feed system can be easily removed from the molding, leaving little trace of its presence. Flow conditions in the gate are extremely severe. The melt is accelerated to a high velocity and is subjected to a high shear rate. This is the main reason for keeping gates short. The gate length is often referred to as the land length; for polypropylene the dimension should be about 0.030 in or 0.75 mm. If the gate land is very short, there will be a weak section in the mold between the runner and cavity, and there will be insufficient clearance to use cutters for gate removal. During the passage of the melt through the gate frictional heating is likely to occur and indeed is sometimes exploited in the design of feed systems for heat-sensitive

Injection molding

182 materials. Here the strategy is to keep barrel temperatures low and generate additional heat at the last moment in the feed system. Many different gate types (Figure 14.28) have evolved to deal with a variety of molding needs. Some of these are associated with particular geometries. For example, diaphragm and ring gates are usually employed for parts with a cylin-

Figure 14.28 Examples of various gate types.

Injection molding

drical form. The pin-point gate is normally used in 3-plate molding. The commonest gate type is the edge gate. The edge gate is usually square or rectangular in cross section and is cut in just one parting face of the mold. Circular section gates are also used but must be cut equally in both parting faces. Semi-circular section gates are not recommended. Gate dimensions depend on product geometry and are frequently adjusted by trial and error during the testing of a new mold. The only practical way to do this is to start with a small gate and gradually enlarge it. As a rough rule, the gate size for polypropylene should be about half the maximum wall thickness of the molding, and should not be less than 0.030 in or 0.75 mm. This dimension is the diameter of a full-round gate or the inscribed circle of a square gate. Simple large area parts in single-cavity molds may be gated by running the sprue directly into the cavity. This is known as sprue gating or direct sprue gating. The gate must be removed in a subsequent machining operation that leaves a witness mark. The sprue gate is perhaps the least sophisticated way of dealing with this type of molding. Fan gates are preferred for thin-walled parts of relatively large area. The flash gate, a variant of the fan gate, is used for thin-walled parts that would be difficult to fill from individual gates at any point. The flash gate is very wide and shallow so that a large flow area is combined with a short freeze time. Ring and diaphragm gates are similar in concept to the flash gate. They are normally used to obtain cylindrical parts free of weld lines and core shift caused by unbalanced flow. The submarine gate, also known as the tunnel gate, is cut into the one half of the mold rather than on a parting face. This constitutes an undercut which is freed on ejection by the runner and gate flexing. The advantage of the submarine gate is that the feed system is automatically separated from the mold by the act of ejection that shears the gate off. Because polypropylene is not a highly rigid material, the inclination of the submarine gate is not critical; angles of 30° to 40° will be suitable. The winkle or cashew gate is a variant in which the gate is machined in a curved form and is suitable only for flexible grades. A further gate type known as the tab gate is used to prevent jetting into an open cavity or when some defect is expected close to the gate. The tab is a small extension on the molding which is fed at right angles to its axis by an edge gate; the tab is later removed from the finished part.


183 14.4.4.4 Hot runner Hot runner systems maintain the feed channels in a permanently molten state and so eliminate the waste associated with a solidified cold feed system. Another advantage is that the pressure drop through the feed system is less than that of a comparable cold runner arrangement. The principal disadvantage is the need to maintain two very different temperature regimes within the mold. The hot runner system in a polypropylene mold may be operating at 260°C in close proximity to mold cavities at 20°C. This results in difficult problems of temperature control and differential expansion. The cost of a hot runner mold is also much greater than that of the cold runner equivalent. However, the important point is not the cost of the mold but that of the molding and here hot runner molds have the advantage. Unless order quantities are low or frequent color changes are required, there are grounds to prefer the hot runner mold. Processors are still often deterred by control and engineering fears associated with hot runners, but there has been great progress in this area, and very sophisticated and reliable designs are now available as stock components. Most manufacturers of hot runner components now offer completely engineered systems that free the molder and mold builder from design responsibility. Traditionally, cold runner molds have been the norm and hot runners the exception but progress has been such that the project concept really should now start from the opposite premise. The heart of a hot runner system (Figure 14.29) is the manifold. This is a distribution block containing flow channels maintained at melt temperature. The channels distribute the melt from the single entry point at the sprue to multiple outlets at nozzles that feed individual cavities in a multicavity mold or serve as multiple gates in a single

Figure 14.29 Schematic of hot runner mold.

large cavity. The latter case is one of the most important applications of hot runners; multiple gates allow the flow lengths in a large part to be brought within easily manageable proportions. The same strategy also limits the necessary clamp force. Contact between the hot manifold and the remainder of the cool mold must be kept to a minimum to prevent heat flow. This is normally achieved by the use of air gaps that also allow for expansion, but care must be taken in the design to ensure that the mechanical strength of the mold remains adequate to deal with molding and clamping forces. The heat transfer problem is reduced with internally heated hot runners but the disadvantage is the relative inefficiency of the annular flow channel. These channels have higher pressure drops than unobstructed channels and are also prone to “slow flow” areas where material may stagnate and decompose. Internally heated hot runners are not on the whole recommended for

Figure 14.30 Some types of direct hot runner gate.


Injection molding

184 use with polypropylene. A primitive variant of the hot runner is known as an insulated runner. This employs an unheated manifold with very large runners of 20 mm to 35 mm (0.75 in to 1.375 in) diameter, and relies on the poor thermal conductivity of plastics to ensure that a flow channel in the center of the large runner always remains molten. The insulated runner mold is not capable of precise and consistent control and is now rarely seen. The connection between the hot runner manifold and the cavity is made by means of a hot nozzle that may operate in conjunction with a surrounding bushing. A wide variety of nozzle types allow for many gating options (Figure 14.30, Figure 14.31), with or without witness marks. Hot runner nozzles may be provided with shut-off valves for precise control of flow. In recent years, great progress has been made in the design of hot runner nozzles for small and closely spaced cavities. These designs allow one nozzle to feed a number of cavities, and also permit gating options that are almost undetectable on the finished part. Polypropylene is not a particularly demanding material for hot runner applications. Most recommendations would be good practice with any thermoplastic. The heating power for manifolds should be at least 60 to 80 watts per cubic inch of

Figure 14.31 Advanced hot runner gates.

steel, and heaters should be positioned to eliminate hot and cold spots. Manifold flow channels should be at least 12 mm (0.5 in) in diameter. Large manifolds and high shot volumes will need bigger channels. Flow channels should be streamlined to prevent slow or stagnant flow. Corners should be radiused by contoured end plugs. The manifold air

Table 14.11 Comparison of properties of some mold construction materials.

Alloy type

Thermal conductivity (W/m.K)

Alloy UNS number

Rockwell hardness

Tensile strength (MPa)

STEEL Type 420 stainless steel

S42000

24.9

C27 — C52

863–1725

H–13 tool steel

T20813

24.9

C38 — C54

1421

P–20 tool steel

T51620

38.1

C28 — C50

1007

ALUMINUM Type 6061 T6

A96061

166.9

B60

276

Type 7075 T6

A97075

129.8

B88

462

COPPER Aluminum bronze

C62400

62.3

B92

725

BeCu — high hardness

C17200

104.8

C41

1311

BeCu — Moderate hardness

C17200

131.0

C30

1173

BeCu — High conductivity

C17510

233.6

B96

759

C18200/18400

325.5

B60 — B80

352–483

NiSi — Hardened copper

C64700

162.6

B94

725

NiSiCr — Hardened copper

C18000

216.3

B94

690

Cr — Hardened copper

Injection molding


185 gap should be at least 1.5 mm (0.62 in). Manifold support pads should have minimal surface contact and should be furnished in materials of relatively low thermal conductivity such as stainless steel or titanium. Precise temperature control is necessary for consistent results. The temperature of the manifold block should be uniform throughout. Each nozzle should be provided with individual closed-loop control. 14.4.5 Injection Mold Features 14.4.5.1 Materials Injection molds are subject to rigorous requirements that have a direct bearing on the materials of construction (Table 14.11). Mold materials must withstand high injection pressures and clamp forces. They must be good thermal conductors, easy to machine, and be capable of reproducing fine detail and taking a high polish. They must be resistant to corrosion, abrasion, and wear. The traditional answer has always been steel and over the years the choice of alloyed and sintered steels

available to the mold maker has steadily expanded. Some are used only in specialist applications while others are generally used just for specific parts of the mold. Indeed, the average modern injection mold will contain a number of different steel types, some in the “as machined” state and others in a hardened and tempered condition (Table 14.12). The choice of alternatives to steel is also growing, and the principle candidates are aluminum and copper alloys. There are two main reasons for using one of these materials in place of steel. They are generally softer and easier to machine. This speeds up mold production and reduces costs. The second reason is that they have much greater thermal conductivity than steel. This property can be exploited in areas of the mold where it is difficult to engineer adequate cooling channels or when a high rate of heat transfer is required for rapid cycling. The principal disadvantage is that these materials are much less hard and strong than steel alloys. Molds using aluminum and copper alloys are far more prone to damage

Table 14.12 Applications of principal mold steels. Werkstoff number

DIN description

Rockwell hardness

Medium carbon steel

1.1730

C45 W3

C10

Unhardened parts Back plates Cavity and core holder plates

Pre-hardened For high compressive sulfur-free tool stresses. Good for steel spark erosion. Not recommended for high polish.

1.2311

Cr Mn Mo7

C32

Cavity and core holder plates Cavity and core inserts

Pre-hardened For high compressive sulfur-free tool stresses. Good for steel spark erosion.

(AISI P20)

Type

Pre-hardened tool steel

Characteristics

Applications

C30 — C32 Cavity and core holder plates Cavity and core inserts

For high compressive stresses. Not recommended for high polish.

1.2312

40 Cr Mn MoS 86

ThroughHigh toughness. High hardening tool resistance to wear and steel corrosion. Suitable for mirror-finish polish.

1.2767

X45 Ni Cr Mo4

Pre-hardened stainless steel

High resistance to corrosion. Suitable for mirror-finish polish.

1.2316

X36 Cr Mo 17

Throughhardening stainless steel

High resistance to corrosion. Suitable for mirror-finish polish.

1.2083

X42 Cr 13 (AISI 420)

C48 — C53 Cavity and core inserts

1.2344

X40 Cr Mo V–51 (AISI H–13)


ThroughGood dimensional hardening hot- stability in heat work tool steel treatment


C32

Cavity and core holder plates Cavity and core inserts Support plates


C30

Cavity and core inserts

Injection molding

186 and are rated for a shorter production life than a steel mold. Some of the latest materials are closing the gap on steel to a limited extent. Steels too can vary in thermal conductivity. Stainless steels are substantially inferior in this respect to normal alloys and this can prove a major handicap in molds with high thermal requirements. The tables compare the main materials of mold manufacture, and outline the uses of the leading mold steel types. Polypropylene is normally non-corrosive in contact with all common mold steels, but a few cases of corrosion have been reported, particularly at vents. Provided cavities and cores are produced in an alloy with a chromium content of 10% or more, there should be no difficulty. Polypropylene can itself be affected by copper alloys. These can induce degradation and should not be used in hot runner components that are in direct contact with the melt. However, there should be no difficulty in using copper alloys for cavity and core components because the melt is rapidly cooled on contact. Indeed, it is the high heat extraction demand posed by polypropylene that has the most direct bearing on the choice of mold material. Stainless steels should be avoided, and if there is any difficulty in engineering adequate cooling channels, then high thermal conductivity materials should certainly be used. 14.4.5.2 Cooling It is a fundamental requirement of the injection mold to extract heat from the molding. With each cycle, the mold acts as a heat exchanger to cool the injected material from melt temperature to at least ejection temperature. The efficiency with which this is done has a direct bearing on speed of production. Heat is removed from the injection mold by circulating a fluid coolant through channels cut through the mold plates and particularly through the cavities and cores (Figure 14.32). The coolant is usually water but may be an oil if the mold is to be cooled at temperatures near or above the boiling point of water. Such a mold appears hot in relation to the ambient temperature, but it is still cold compared to the plastics melt. If the mold is to be chilled at low temperatures, it is usual to circulate a mixture of water and ethylene glycol antifreeze. Occasionally the coolant may be air, but this is an inefficient means of heat transfer and should be regarded as a last resort.

Cooling channels represent a real difficulty in mold design. Core and cavity inserts, ejector pins, fasteners, and other essential mechanical features all act as constraints on the positioning of cooling channels, and all seem to take precedence over cooling. However, uniform and efficient cooling is crucial to the quality and economy of the molding, so channel positioning must take a high priority in mold design. Cooling channel design is inevitably a compromise between what is thermally ideal, what is physically possible, and what is structurally sound (Figure 14.33). The thermal ideal would be flood cooling over the entire area of the molding, but the pressurized mold cavity would be unsupported, and mechanical details like ejectors could not be accommodated. Support could be provided by interrupting the flood cooling chamber with supporting ribs, but the mold construction is complicated by the need to fabricate and seal the cooling chamber. The reasonable and practical compromise provides the cooling channels in the form of easily machined through bores that may be linked either inside or outside the mold to form a complete cooling circuit. The correct placement of the channels is important. If they are too widely spaced, the result is a

Figure 14.32 Cooling arrangements for cores of various sizes.

Injection molding


187 mensionless number given by the equation:

Re =

Figure 14.33 Cooling channel considerations.

wide temperature fluctuation over the cavity or core surface (Figure 14.34, Table 14.13). If the channels are too closely spaced or too close to the cavity surface, the mold becomes structurally weak. Another important consideration in cooling channel design is to ensure that the coolant circulates in turbulent rather than laminar (streamline) flow. The coefficient of heat transfer of the cooling system is drastically reduced in laminar flow. The condition of laminar or turbulent flow is determined by the Reynolds number (Re). This is a di-

Dvρ η

where D = channel diameter, v = coolant velocity, ρ = coolant density, and η = coolant viscosity For a channel of circular cross-section, turbulent flow occurs when the Reynolds number is greater than 2,300. The coefficient of heat transfer of the cooling system continues to increase as turbulence increases, so the design limit of the Reynolds number for cooling channels should be at least 5,000 and preferably 10,000. If the volume flow rate of the coolant remains constant, then the Reynolds number can be increased by reducing the size of the channel. This runs counter to the natural impulse to image that a larger channel must always result in better cooling. It is harder to achieve turbulent flow with oils or anti-freeze solutions because of their greater viscosities compared with water. Good cooling channel design is particularly important for molds to be used with polypropylene. The material has the highest heat content to remove on cooling of any thermoplastic with the exception of high density polyethylene. This means that slender cores and corners will rapidly and inevitably heat up unless special attention is paid to cooling by means of extensive coolant circulation coupled with the use of heat pipes and high thermal conductivity mold materials. As a general rule, it is impossible to design too much cooling into a polypropylene mold. 14.4.5.3 Venting When an injection mold fills, the incoming highvelocity melt stream is resisted by and must displace the air in the feed system and cavities. Molders often rely on incidental air gaps between the parting faces and between the assembled parts of the core and cavity to provide a leakage path for air, but this is no substitute for properly engineered venting which should be designed into all molds Table 14.13 Recommended cooling channel dimensions for polypropylene (refer to Figure 14.34).

Figure 14.34 Bad and good cooling channel layouts.


Wall thickness w (mm)

Channel diameter d1 (mm)

Channel spacing b (mm)

Channel depth c (mm)

–

–

–

–

Melt temperature

–

–

Roll temperatures

–

>

>

13.5)b

50 (0.3)

200 (1.4)

100 (0.7)

Roughened 26 rms

50 (0.3)

550 (3.8)

1300 (9.0)

300 (2.1)

200 (1.4)

450 (3.1)

Antioxidant 0.1% Irganox 1010 0.3% Cyanox STDP

50 (0.3)

250 (1.7)

>1950 b (>13.5) b

50 (0.3)

200 (1.4)

100 (0.7)

UV stabilizer

0.5% Cyasorb UV 531

50 (0.3)

50 (0.3)

>1950 b (13.5) b

50 (0.3)

200 (1.4)

100 (0.7)

Impact modifier

9% Novalene EPDM

50 (0.3)

150 (1.0)

>1650 b (>11.4) b

200 (1.4)

200 (1.4)

100 (0.7)

Flame retardant

9% PE-68 4% Antimony oxide

50 (0.3)

50 (0.3)

>1950 b (>13.5) b

50 (0.3)

200 (1.4)

250 (1.7)

Smoke 13% Firebrake ZB suppressant

50 (0.3)

50 (0.3)

>1950 b (>13.5) b

50 (0.3)

200 (1.4)

100 (0.7)

Lubricant

0.1% Calcium stearate 24-26

50 (0.3)

50 (0.3)

>1950 b (>13.5) b

50 (0.3)

200 (1.4)

100 (0.7)

Filler

20% Cimpact 600 Talc

50 (0.3)

50 (0.3)

>1950 b (>13.5) b

100 (0.7)

200 (1.4)

100 (0.7)

Colorant

0.1% Watchung Red RT-428-D

50 (0.3)

50 (0.3)

>1950 b (>13.5) b

50 (0.3)

200 (1.4)

100 (0.7)

Antistatic

0.2% Armostat 475

50 (0.3)

200 (1.4)

>1950 b (>13.5) b

200 (1.4)

200 (1.4)

100 (0.7)

Plastic Material Composition (Himont Profax 6323) Unfilled resin

a b

c

5 rms

Super Bonder 414 Depend 330 general purpose two-part nocyanoacrylate mix acrylic (110 cP)

Loctite 3105 light cure acrylic (300 cP)

All testing was done according to the block shear method (ASTM D4501). Due to the severe deformation of the block shear specimens, testing was stopped before the actual bond strength achieved by the adhesive could be determined (the adhesive bond never failed). For more information on data presented in this table, contact Loctite Corporation at 800-562-8483 (1-800-LOCTITE). Request the “Design Guide for Bonding Plastics.”

18.1.14 Mechanical Fastening Mechanical fastening is a simple and versatile joining method. Mechanical fasteners are made from plastics, metals, or a combination of the two materials and can be periodically removed and replaced or reused when servicing of the part is necessary. Screws, nuts, and inserts can be made of plastic or metal; rivets are generally made from metals. Plastic fasteners are lightweight, corrosion resistant, and impact resistant. They do not freeze on threads of screws and require no lubrication. Metal fasteners provide high strength and are not affected by exposure to extreme temperatures. [680] Screws, nuts, washers, pins, rivets, and snaptype fasteners are examples of non-integral attachments, in which the attachment feature is a


separate part. Use of separate fasteners requires plastic materials that can withstand the strain of fastener insertion and the resulting high stress near the fasteners. Snap-fits are examples of integral attachments, attachment features that are molded directly into the part. Strong plastics that can withstand assembly strain, service load, and possible repeated use are required for non-integral attachments. Separate fasteners add to product cost due to increased assembly time and use of additional material and can be difficult to handle and insert; as a result, use of integral attachment features is increasing. [579, 678, 687] Different types of mechanical fasteners are described in the following sections.

Fabricating and Finishing

262 18.1.14.1 Machine screws and nuts, bolts, and washers Parts joined using machine screws or screws with nuts can be disassembled and reassembled an indefinite number of times. Tensile stress should be avoided in assembly design; compressive stress is more desirable due to a lower susceptibility to stress cracking and crazing. [416] Machine screws and bolts used in joining plastic parts should have a flat side under the screw head. Flat head screws, with conical heads, produce potentially high tensile stresses due to wedging of the screw head into the plastic part. Screws with flat undersides, such as the pan head screw, do not undergo this wedging action, and the stress produced is more compressive. Flat washers distribute the assembly force and should be used under the fastener head. [502, 640] Screws or threaded bolts with nuts pass through the plastic part and are secured by an external nut or clip on the other side. For compressive rather than tensile loading, space between surfaces of parts being assembled should be eliminated, using spacers if necessary. Some part designs may require a loosefit gap between bosses to prevent high bending stresses or distortion as the parts go into compression. [78, 639, 430] 18.1.14.2 Self-tapping screws Self-tapping or self-threading screws cut or form a mating thread in a preformed hole of a plastic part. No nuts are used, and access is needed from only one side of the joint. No clearance is required, since the mating thread fits the screw threads. Only a drilled or molded pilot hole is required, and installation is rapid. Self-tapping screws are widely

used due to an excellent holding force and lower stress production than some of the other fastening methods. [629, 678, 639, 676] The two basic classes of self-tapping screws for thermoplastics are thread-forming screws and thread-cutting screws. Thread-forming screws form threads in the plastic by displacing and deforming plastic material, which flows around the screw heads. No material is removed, which creates a fit with zero clearance and produces large internal stresses. Thread-forming screws are inexpensive and vibration resistant. They are recommended for structural foam parts. Although they can provide acceptable performance in solid-wall parts, they should be used with caution in nonfoam materials due to the possible generation of highly stressed regions. Multiple assemblies and disassemblies are possible with thread-forming screws. [678, 674, 118] Thread-cutting screws have a sharp cutting edge; as the screw is inserted, plastic chips are removed. Depth of the preformed hole should be slightly longer than the screw depth in order to provide a depository for the plastic chips. High internal stresses are avoided in thread-cutting screws due to removal of material during installation. Stress relaxation of the plastic with temperature changes and time has only a minimal effect on screw performance. Only a minimum number of reassemblies are possible; repeated removal and reassembly may cause new threads to be cut over the original thread, resulting in a stripped thread. For repeated assembly, the screw should be carefully inserted into the original thread by hand, or Type 23 screws (Figure 18.16) should be used initially and replaced with a standard machine screw for reassembly. Thread-

Figure 18.16 Common types of self-tapping screws.



263 cutting screws provide acceptable performance in solid-wall parts but are not recommended for structural foam. [640, 678, 674, 78, 676] Different types of thread-forming and threadcutting screws are available for particular applications. The most widely used self-tapping screws for thermoplastics are the Type B, Type BT, Hi Lo, and Trilobe or Plastite. Type B, a thread-forming screw is otherwise identical to Type BT, a threadcutting screw (Figure 18.16). The Hi Lo is a double-lead screw, available as either thread-forming or thread-cutting; the Trilobe is a thread-forming screw with triangular-shaped threads. [674] 18.1.14.3 Inserts Inserts are plastics or metals that are inserted into another material. They are commonly used for applications that require frequent disassembly, or when a limited engagement length prevents the use of screws. They are used for structural foam and other materials with low shear strengths that cannot withstand fastener loads alone. Threaded inserts are available in internal thread sizes from 440 to 1/4–20 (inches) or M2 — M6 (metric). Various lengths are available in each size for different depths. Performance of inserts is dependent on the shear strength of the material and the knurl pattern on the outer surface of the insert. [674, 678, 501] Molding inserts directly into the part during the injection molding process is a convenient and popular method of insert application. Molded-in inserts provide an anchor for machine screws and are commonly made from metals such as steel, brass, and aluminum. Inserts are placed on core pins in the mold, and the plastic part is then molded around them in the mold cavity. Molding in inserts does not require a secondary insertion operation and provides higher torque and pull-out properties than other insertion methods; however, high stresses are created in the areas around the inserts. [623, 122, 678] Molded-in inserts are not recommended for use with some plastics because of the high stresses produced. Molded-in inserts perform better in higher creep, cyrstalline polyolefins than with rigid amorphous resins. Molded-in stresses result in high failure rates in the form of cracking in low creep materials. [623, 500] Processing conditions can affect the quality of the molded-in insert. In experiments with polypropylene homopolymer, the pull-out resistance of molded-in inserts was sensitive to changes in injec-


tion pressure, injection time, and insert temperature. Increases or decreases in injection pressure or injection time from the optimum values, with all other processing parameters identical, significantly decreased holding power in tensile tests. Increasing the insert temperature to 95°C from 22°C reduced the load required to pull the insert out of the surrounding plastic material by 19 kg. [681] Holding power was dramatically reduced when internal lubricants (epolene wax, calcium stearate) were used in molding. Lubricants were present at loading levels recommended by the manufacturers. The pull-out load for inserts in polypropylene decreased by 29 and 37 kg in the presence of epolene wax and calcium stearate, respectively. Lubricants caused the inserts to slip out of the plastic more easily. Mold Wiz lubricant did not affect pull-out resistance as dramatically; the decrease in load required for pull-out was 9.5 kg. [681] Expansion inserts have longitudinal slots that collapse on installation to allow the insert to enter the preformed hole. Once in place, the insert can be expanded by either a spreader plate incorporated into the insert or by the action of the assembly screw. Because these inserts absorb much of the assembly force, they are used in plastics that cannot withstand a high level of stress. [679, 495] Self-tapping inserts have coarse threads and longitudinal slots or notches that cut into the plastic material. When the insert is screwed in, a corresponding thread is produced in the plastic. Selftapping inserts provide high pull-out resistance but poor torsional resistance. [495] Thermal inserts are heated before insertion into the plastic material. The heated insert softens the plastic, which then flows around the outer surface of the insert. Thermal heating can occur by direct contact with a hot body or by preheating in a temperature-controlled chamber. Installation equipment is inexpensive, but insertion is slow. [674, 495] 18.1.14.4 Press or interference fits In press or interference fits, a shaft of one material is joined with the hub of another material by a dimensional interference between the shaft outside diameter and the hub inside diameter. Press-fitting is an economical procedure that requires only simple tooling, but it produces very high stresses in the plastic parts. It can be used to join parts of the same material as well as dissimilar materials. [118, 500, 78] Maximum pull-out forces are obtained in press fits by using the greatest allowable interference


264 between parts that is consistent with the strength of the materials. Allowable interference is dependent on the properties of the materials, part geometry, and environmental conditions. Interference limits are determined for a part design to ensure that the hoop stress produced in the parts does not exceed the maximum allowable stress for the plastic. [629] The high stress produced in press fit assembly can make the parts more susceptible to chemical and thermal attack. To reduce stress concentrations, parts and inserts should be clean and free of all incompatible chemicals. Inserts with smooth, rounded surfaces produce less stress than knurled inserts, and knit lines should not be located in areas of the part that are being inserted. [500, 502, 78] 18.1.14.5 Snap-fits In snap-fit fastening, two parts are joined through an interlocking configuration that is molded into the parts. Many different configurations are possible to accommodate different part designs. In snap-fits, a protrusion on one part (hook, stud, bead) is briefly deflected during joining to catch in a depression or undercut molded into the other part. The force required for joining varies depending on the snap-fit design. After the brief joining stress, the joint is vibration resistant and usually stress-free. [502, 675, 78] Snap-fitting is an economical, rapid, and popular assembly method. Snap-fits can be used to join dissimilar plastics or plastics to metals and can be designed for permanent fastening or for repeated disassembly. Hermetic or moisture-resistant seals are possible in some designs. Snap-fits require more attention to engineering design than other mechanical fastening methods and can fail before or during assembly or during use if not designed properly. Stress analysis of some snap-fit designs can be performed using hand calculations; designs with more complicated geometries may require finite element analysis for accurate results. [579, 690] The most common type of snapfit is the cantilever beam. A cantilever beam snap-fit is a hook and groove joint, in which a protrusion from one part interlocks with a groove on the other part (Figure 18.17). Cantilever beam snap-fits can be straight or may have a bend in the beam (curved beam). Rectangular cross-sections are common; beam cross-sections may also be square, round (hollow or filled), trapezoidal, triangular, convex, or concave. The beam can be of constant width and height or can be tapered to avoid stress con-


Figure 18.17 A cantilever beam snap-fit. a) A cantilever beam and mating piece before assembly. b) The latch is partially deflected as initial contact is made. c) The latch approaches maximum deflection. d) The latch locks into the hole in the mating part and returns to its undeflected position.

centration near the point of attachment with the part wall. [675, 502] Cantilever snap-fits are easy to assemble and provide good retention. They undergo flexural stress during assembly and are modeled as cantilever beams in design calculations. After assembly, joints are usually stress-free; however, joints can be designed to be partially loaded after assembly for an extra-tight fit. Loaded snap-fits may be subject to creep or stress relaxation. [629, 690] Other types of snap-fits include annular, used to join spherical parts, torsional, in which a latch is attached to a torsion bar or shaft; ball and socket snapfits, used to transmit motion; and U-shaped snap-fits, commonly used for lid fasteners. Combinations of different types are also possible in one design. Some design considerations in snap-fits include the forces required for assembly (and disassembly, if required), ease of molding and assembly, the material strain produced during assembly, and other requirements of the application. Stress analysis, based on a geometric model for the particular type of snap-fit, is performed to determine assembly forces, deflections, and stresses produced during assembly. [579, 675] Snap-fits are used in a variety of industries to assemble power tools, computer cases, electronic components, toys, automobile parts, medical devices, washing machines, pens, bottles, and packaging boxes. Snap-fits can be used as a temporary holder for other assembly methods, such as adhesive bonding or welding. [690]


265 18.1.14.6 Staking In staking, a head is formed on a plastic stud by cold flow or melting of the plastic. The stud protrudes through a hole in the parts being joined, and staking the stud mechanically locks the two parts together (Figure 18.18) [681] Staking can be performed by four different methods: ultrasonic staking, cold staking, heat staking, and thermostaking. Cold staking or heading uses high pressures to induce cold flow of the plastic material; pressures of at least 41 MPa (6000 psi) are generally required. Stud lengths are approximately 1.5 times the stud diameter; stud length includes part thickness. Because cold heading creates high stresses on the stud, only more malleable thermoplastics are suitable for this process. Soft, brittle, or fragile materials are not usually assembled by cold staking. [681] In heat staking, heated probes and light to moderate pressure are used to compress and reform the stud. Because stresses are lower than in cold staking, heat staking can be used to join a variety of plastic materials; polypropylene is commonly used for heat staking. Heat staking is used to join two parts of the same plastic or dissimilar plastics. It is an economical process that produces consistent results. [677, 681] Thermo-pneumatic staking or thermostaking uses a heated, hollow tool to deliver a low volume of superheated air to the plastic stud. The tool is

lowered over the stud, and the hot air rapidly softens the plastic. The hot air flow is then shut off, and a cold stake probe located at the top of the tool descends onto the stud. A stud head is formed, and, after the plastic solidifies and cools, the cold staking probe is retracted. [681, 495] In ultrasonic staking, a thermoplastic stud is melted and reformed to mechanically lock another, usually dissimilar material in place. A thermoplastic stud protrudes through a hole in the dissimilar material, usually metal; ultrasonic energy melts the stud, which compresses under pressure from the horn and takes the shape of the horn cavity. After vibrations stop, the horn remains in contact with the stud until it solidifies. Ultrasonic staking works well with soft or amorphous materials having low melt flows, allowing the head of the rivet to form by both mechanical and thermal mechanisms. With high melt materials or materials that require high vibrational amplitudes, melt can flow so rapidly that is is ejected out of the horn contour, resulting in an incomplete rivet head. [532, 619]

18.2 Decorating Plastics decorating involves the modification of a plastic surface, using a coating or impression, by the application of heat, pressure, or a combination of both. Several decorating techniques are described below. 18.2.1 Appliqués Appliqués are surface coverings applied using heat and pressure for a specified period of time; they may be applied as decals, during molding, or by hot stamping, hot transfer, or water transfer. 18.2.1.1 Decals Decals are decorations or labels printed on carriers such as paper or plastic with a pressure sensitive adhesive backing. The decal is pressed into place on the plastic part when the backing is removed. Decals require a clean surface, free of mold release agents, with minimal sink marks and projections, and the adhesive backing must be compatible with the plastic. Gate marks should be hidden, and sharp corners should be broken to 0.5 mm (0.020 in.).

Figure 18.18 Staking. A plastic stud protruding from the part is softened by heat or forced to cold flow by high pressure, forming a mushroomed stud head that locks the parts together.


18.2.1.2 Hot stamping In hot stamping, a pigmented, metallic or wood grain foil is placed between an etched metal or rubber die and the plastic surface. The etched pattern is


266 the reverse of that desired on the plastic. Heat, pressure, and a specific dwell time is then applied to stamp the pattern onto the surface. Foils are multilayer laminates whose composition depends on the physical properties of the foil material (mar and chemical resistance, color) and properties of the plastic material (melt profile, surface characteristics). Foils are usually developed for the particular plastic and sometimes for the particular grade. 18.2.1.3 Hot transfer In hot transfer, a dry coating is transferred to the plastic surface through a heated die; however, in this method, the die is flat, while the carrier contains the decorative pattern. 18.2.1.4 Water transfer In water transfer, a flexible, water-soluble carrier film with an imprinted pattern is floated, ink side up, on the surface of a water bath. The plastic part is then dipped into the bath, and the film conforms to the shape of the part. After removal of the part, the film washes off, and a transparent coating is applied for abrasion resistance. Water transfer is used for patterns with no definite orientation (wood grain, marbling) and can be used on curved, contoured, and rough surfaces and around corners. The method requires a clean surface; application of a primer before decorating improves adhesion and properties. Projections on the part must be minimized, and no holes should be present. 18.2.1.5 In-mold decorating Parts can be decorated during molding by placement of a predecorated carrier into the mold; the molten plastic then fuses with the film during processing. Carriers must have good thermal stability due to the high temperatures encountered in injection molding. There should be no sharp edges, and complex surfaces may result in problems caused by air entrapment or stretching of the film. 18.2.2 Coloring Colors can be blended or molded into the plastic resin; parts with contrasting outlines are produced with two molding sequences — one shot to provide a frame or core and the second for the complementary color. In two-color molding, sharp corners and edges should be minimized. The same material should be used for both part elements, and cycle time between molding of the two parts should be minimized.


Surfaces can be dyed by immersion of the part into the dye. Dyeing is an economical process, useful if abrasion resistance is unnecessary; however, uniformity is hard to control, and the maintaining of outlines is poor. Clean surfaces are necessary, with uniform walls and well-rounded edges for projections. 18.2.3 Painting Parts can be painted to provide color for color matching, a high gloss or matte finish, a wood grain, luminescent or metal flake appearance, a textured appearance, or coverage of surface imperfections. Paints and coatings can also provide enhanced performance properties such as improved chemical, abrasion, or weathering resistance and electrical conductivity. Painting requires clean surfaces, and the paint should be compatible with the substrate. Parts should have uniform walls, and molding should be stress-free. 18.2.4 Metallization Plastic surfaces are metallized to give the material surface a metallic appearance and make its properties more similar to that of a metal. Conductive paints composed of pigments and conductive particles (nickel, copper, silver, graphite) can be applied to the part with air atomizing or airless spray equipment. In electroplating, electric current is used to deposit metals from a metal salt solution onto a plastic rendered conductive by electroless plating. Flame/arc spraying uses a jet of compressed air to atomize molten metal particles, obtained by melting metal wires with an electric arc, and spray them onto the part surface. In vacuum metallizing, the metal is heated in a vacuum chamber to its vaporization point, which is lower than the melt temperature of the plastic. The metal vapor then condenses on the cooler plastic surface. Sputtering is a process in which metal atoms are dislodged by contact with an inert gas plasma instead of by heating the metal. In cathode sputtering, the metal is attached to the cathode, with the plastic acting as the anode. An electron beam dislodges positively charged metal ions, which then condense on the plastic surface. Ion plating is similar to sputtering, but inert gases are also used, in order to enhance adhesion from a chemical reaction of the inert gas plasma and the substrate. Metallizing makes surface flaws more apparent, and the resin’s physical characteristics may change. Clean surfaces are required, with no mold


267 release agents present, and pre-cleaning processes should be checked for compatibility. Design considerations include: uniform wall sections radiused sharp edges and corners (0.5 mm; 0.020 in. minimum) avoidance of deep vertical walls gradual wall transitions minimal amount of projections avoidance of flat areas hole depth of a diameter ratio less than 5 to 1 recesses less than 5.1 cm (2 in.) with greater than 5 degrees draft minimum wall thickness about 2.0 mm (0.080 in.) maximum walls ranging to 4.8 mm (0.190 in.) 18.2.5 Printing In printing, a mark or impression is made on a plastic surface. Printing processes include pad transfer, screen printing, laser printing, dyeing, and fill and wipe. In fill and wipe processes, the part is etched, and ink is used to fill the recesses. Excess ink is then wiped away. For sharp detail, the surrounding surface should be very smooth, and edges should be sharp. Adjacent surfaces should be polished. Thick rather than thin borders should be used, and inside corners should be radiused. Recesses should be 0.38 to 0.76 mm (0.015–0.030 in.) deep; small character openings may not be filled in. Pad transfer is used to print on flat or irregular surfaces. A metal plate with an etched pattern is covered with ink, and a soft silicone rubber pad is pressed onto it. The pad picks up the ink pattern (in reverse) and is pressed against the part. The pad can wrap 180° around a small part (360° with specialized equipment), and coverage is excellent. Parts for pad transfer decorating should be designed with smooth and even transitions, and sharp edges and projections should be avoided. The surface finish affects sharp line intersections, and thickness can be inconsistent in large print areas. The size of the printing area should be minimized. In screen printing, a pattern is produced by selectively sealing holes in a fine mesh screen. The screen is then placed on the part, and a squeegee is used to force ink through the open holes onto the part surface. Parts should be designed with smooth and even transitions, with all coverage areas in one plane, and points and projections should be avoided.


In diffusion processes (wet or dry), dye solids are transferred below the surface of a plastic (to a depth of 0.025–0.100 mm; 0.001–0.004 in.) using heat or heat and pressure. Inks used in this process undergo sublimation — they change from a solid to a gas and back without passing through the liquid phase. In wet diffusion, pad transfer methods are used to transfer the inks from a solvent suspension, which evaporates after exposure to heat, to the plastic substrate. Dry diffusion is similar to hot stamping; designs are reverse printed on a carrier, then applied to the surface by heat and pressure over a period of time. Wet diffusion is more economical; however, dry diffusion can transfer multiple colors in one operation. Since dye inks are translucent, diffusion is appropriate only for light colored surfaces. Diffusion methods are limited to parts having planar or slightly curved surfaces, and the surface finish affects sharp line intersections. Wall sections should be thick enough to be stable during the heating process of dry diffusion. Laser printing uses a CO2 or YAG laser to produce marks on the surface. The laser beam vaporizes the plastic surface, changing the color. It is useful for permanently coding parts too small for conventional printing processes. Pulse power, rate, and marking speed control the depth of etching; the amount of contrast produced is important in determining the quality of the finish. Design considerations include gradual wall transitions and a minimization of sink marks. 18.2.6 Other processes Textures and lettering can frequently be molded into the surface of the part, in order to hide surface imperfections and provide decoration at no additional cost. Additional draft is required to eject a part with textured sides. Surfaces with molded-in texture do not usually maintain optical clarity. Another special process is flocking, in which the surface is coated with an adhesive and exposed to an electrostatic charge. Short textile fibers are then blown onto the surface and stand on end due to the charge. As in other processes, flocking requires clean surfaces, with a minimal amount of sink marks, wall transitions, and projections. Sharp corners should be broken to a minimum of 0.5 mm (0.020 in.). [959]


268

19 Polypropylene Data Collection 19.1 Data Sheet Properties Material family

polypropylene homopolymer

Supplier

polypropylene polypropylene polypropylene polypropylene, polypropylene, polypropylene, homopolymer, homopolymer, homopolymer, 10% talc 20% talc 20% talc, flame retardant fibers cast film easy-flow

BASF

Vestolen GMBH

Vestolen GMBH

BASF

Hoechst

Hoechst

Hoechst

Material Trade Name

Novolen 1100L

Vestolen P 7006 S

Vestolen P 4000

Novolen 1127 N

Hostacom M1 U01

Hostacom M2 N01

Hostacom M2 U01

Source ID

756, CAMPUS

711, CAMPUS

711, CAMPUS

756, CAMPUS

326, CAMPUS

326, CAMPUS

326, CAMPUS

8

3

23

15

20

2.3

18

30

38

4.2

34

85

10

78

Test Notes

Test condition

Test Specimen Test Method

(Unit)

PROCESSING PROPERTIES melt volume rate (230°C, 2.16 kg)

ISO 1133, DIN ml/10min 53735, CAMPUS

melt volume rate (190°C, 5 kg)

ISO 1133, CAMPUS

“

DIN 53479

“

ISO 1133, DIN 53735

g/10min

5

2.4

17.5

11

16

2

16

melt flow rate (190°C, 5 kg)

“

“

9

4.5

33

22

28

3.8

28

melt flow rate (230°C, 5 kg)

“

“

11

80

67

9

67

%


test specimen note: granules

melt flow rate (230°C, 2.16 kg)

molding shrinkage (parallel)

parallel to flow

ISO 2577, CAMPUS

molding shrinkage (normal)

perpendicular to flow

“

processing shrinkage

12

1.3

“ “

molecular weight distribution

GPC

MECHANICAL PROPERTIES tensile modulus (secant, 1 mm/min)

test temperature: 21-25°C; relative humidity: 50%; strain rate: 1 mm/min; elongation: 0.05-0.25%; atmosphere according to ISO 291

stress at yield (50 mm/min)

test temperature: 21-25°C; relative humidity: 50%; strain rate: 50 mm/min; atmosphere according to ISO 291

“

strain at yield (50 mm/min)

“

strain at break (50 mm/min)

“

tensile strength at break (5 mm/min) strain at break (5mm/min) shear modulus

ISO 3167 multiISO 527-1, purpose test ISO 527-2, specimen CAMPUS, DIN 53457

MPa

1500

1500

1650

2300

2500

2600

ISO 527-1, ISO 527-2, CAMPUS, DIN 53455

“

35

34

35

35

32

32

“

“

%

10

8

8

6

6

5

“

“

“

>50

>50

>50

8

20

3

test temperature: 21-25°C; relative humidity: 50%; strain rate: 5 mm/min; atmosphere according to ISO 291

“

“

MPa

“

“

800

850

test temperature: 21-25°C; relative humidity: 50%

“

%

ISO 537, DIN 53445

MPa

750

tensile creep modulus (1 hour)

test temperature: 21-25°C; relative humidity: 50%; elongation: =10 x >=10 x 4 mm

ISO 2039T1, DIN 2039T1

MPa


70

75

78

2.5

5

3

95

81

90

Polypropylene Data Collection

269

polypropylene, polypropylene, polypropylene, polypropylene, polypropylene polypropylene, polypropylene 40% talc 20% glass 20% chemi30% chemiblock block copolyrandom fiber cally coupled cally coupled copolymer mer, UV copolymer glass fibers glass fibers stabilized

polypropylene random copolymer

metallocene polypropylene

metallocene polypropylene, Polypropylene Material family polypropylene elastomerelastomer modified blend recyclate

Hoechst

Hoechst

Hoechst

Hoechst

Vestolen GMBH

BASF

Vestolen GMBH

BASF

Hoechst

Hoechst

Hoechst

Hoechst

Hostacom M4 N01

Hostacom G2 N01

Hostacom G2 U02

Hostacom G3 N01

Vestolen P 7700

Novolen 2660 M

Vestolen P 9421

Novolen 3240 NC

Hostacen XAV10A FOB

Hostacen XAW10A SAB

Hostalen PPN 8018A

Hostalen PP 3100

326, CAMPUS

326, CAMPUS

326, CAMPUS

326, CAMPUS

711, CAMPUS

CAMPUS

711, 712, CAMPUS

756, CAMPUS

709

731

841, CAMPUS

CAMPUS

Supplier Material Trade Name Source ID Test Notes

PROCESSING PROPERTIES 2.5

2

17

1

2.5

10

0.4

16

4.5

3.5

28

2

11

8.5

55

5

2.5

1.7

15

1

1.9

0.3

11

4.5

3.2

23

2

4.5

0.5

22

11

7.5

55

4.5

10

1.5

30

60

30

1.3

9

melt volume rate (230°C, 2.16 kg)

6


35

melt volume rate (230°C, 5 kg) melt flow rate (230°C, 2.16 kg) melt flow rate (190°C, 5 kg) melt flow rate (230°C, 5 kg)

26

molding shrinkage (parallel)

1.3

molding shrinkage (normal) processing shrinkage

0.6-2.0 2.5

2.5

1350

1450

molecular weight distribution

MECHANICAL PROPERTIES 3800

2900

4600

33

33

70

4

8

6

15

6500

3 75

85

4

3

1500

1150

900

1100

30

21

25

28

850

900

tensile modulus (secant, 1 mm/min)

20

18

stress at yield (50 mm/min)

8

6

12

12

10

7

strain at yield (50 mm/min)

>50

>50

>50

>50

>50

>50

strain at break (50 mm/min) tensile strength at break (5 mm/min)

40 {strain rate: 50 mm/min; ISO 527}

strain at break (5mm/min) 650

400

shear modulus

550

2400

2300

3400

4800

1200

550


1200

1300

2400

3200

450

250


30

50

40

40

no failure

no failure

no failure

200

no failure

70

170

50

15

190

9

45

20

6

65

NB

Charpy notched impact strength (23°C)

4.5

6

2.5

1.5

8

5.5

Charpy notched impact strength (-30°C)

no failure

no failure

non-breakable

Izod impact strength (23°C)

65

30

20

Izod impact strength (-30°C)

7

20

6.5

notched Izod impact strength (23°C)

4

2.5

1.5

notched Izod impact strength (-30°C)

3

4.5

9

9

no failure

Charpy impact strength (23°C)

Charpy impact strength (-30°C)

40

40

36

50

notched tensile impact strength

18

50

24

22

impact strength

4

5

7

6

85

80

105

110


notched impact strength 62

70

70

Ball indentation hardness


270 Material family


Supplier

BASF

polypropylene polypropylene polypropylene polypropylene, polypropylene, polypropylene, homopolymer, homopolymer, homopolymer, 10% talc 20% talc 20% talc, flame retardant fibers cast film easy-flow Vestolen GMBH

Vestolen GMBH

BASF

Hoechst

Hoechst

Hoechst

Material Trade Name

Novolen 1100L

Vestolen P 7006 S

Vestolen P 4000

Novolen 1127 N

Hostacom M1 U01

Hostacom M2 N01

Hostacom M2 U01

Source ID

756, CAMPUS

711, CAMPUS

711, CAMPUS

756, CAMPUS

326, CAMPUS

326, CAMPUS

326, CAMPUS

36

38

50 (specimen from compression molded sheet)

45

47

2700

2500

3000

Test Notes

Test condition

Test Specimen Test Method

(Unit)

MECHANICAL PROPERTIES (Continued) Ball indentation hardness flexural stress (3.5% strain)

load: 132 N test temperature: 23°C; relative humidity: 50%

80 x 10 x 4 mm, from injection molded sheet

stress: 12 MPa

120 x 20 x 6 mm, injection molded

creep modulus (flexure, 1 min value) flexural modulus

ISO 2039T1

N/mm2

DIN 53452

“

“

ISO 178

MPa

THERMAL PROPERTIES melting temperature

°C

crystalline melting range

“

163 {DTA or DSC; 10°C/min; ISO 3146, CAMPUS}

163 {DTA or DSC; 10°C/min; ISO 3146, CAMPUS} 164-168 {DIN 53736 B2}

164-168 {DIN 53736 B2}

heat deflection temperature at 0.45 MPa

80 x 10 x 4 mm

ISO 75-1, ISO 75-2, CAMPUS

“

85

85

80


“

“

“

55

55

55


injection molded, 127 x 12.7 x 3.2 mm

DIN 53461; ISO 75

“

Vicat A softening temperature

load: 10N; note: 50°C/h

20 x 20 x 4 mm; from injection molded sheet

ISO/DIN 306, CAMPUS

“

Vicat B softening temperature

load: 50N; note: 50°C/h

>=10 x >=10 x 4 mm

ISO/DIN 306, CAMPUS

“

92

test temperature: 23-55°C

>=10 x >=10 x 4 mm

ASTM E831, CAMPUS

E-4/°C

125 x 13 mm

UL 94, CAMPUS

coefficient of linear thermal expansion (flow direction) flammability UL94 at 1.6 mm flammability UL94 at 1 mm

80 x 10 x4 mm

generic temperature index thermal conductivity

test temperature: 20°C

260 x 260 x 10 mm

“

granules

specific heat

ISO 4589, CAMPUS

%

UL 746B at 1 mm thickness

°C

DIN 52612 method A

W/(mK)

120 {injection 120 {injection molded speci- molded specimen, 127 x men, 127 x 12.7 x 3.2 mm; 12.7 x 3.2 mm; DIN 53461, ISO DIN 53461, ISO 75} 75} 60

70

70

153

153

153

95

95

95

1

1.0 {23-80°C; DIN 53752}

1

90

90

1.35

1

1.5

HB

HB

HB

HB

HB {at 0.8 mm}

HB {at 0.8 mm}

HB

HB

65

65

UL 94, CAMPUS

oxygen index

164 - 167 164-167 {po164-167 {polarizing micro- {polarizing mi- larizing microscope; 20µm scope; 20µm croscope; microtome microtome 20µm microsection} section} tome section}

1.35

0.17

0.37

adiabatic calo- KJ/(kg K) rimeter

0.41 {8 mm 0.41 {8 mm sheet, injection sheet, injection molded} molded}

1.57

1.52

1.49

2.4

2.8

2.8

2.4

2.8

2.8

2.4

2.8

2.8

15

20

20

0.7

15

20

20

2

10

10

10

ELECTRICAL PROPERTIES relative permittivity at 50 Hz

test temperature: 21-25°C; relative plate with diIEC 250, humidity: 50%; atmosphere accord- mensions 1.0 +/- CAMPUS, DIN ing to ISO 291 0.1 mm 53483

relative permittivity at 100 Hz

“

relative permittivity at 1 MHz

“

dissipation factor at 50 Hz (loss factor) dissipation factor at 100 Hz (loss factor)

“

IEC 250, CAMPUS

-

2.3 2.3

“

“

-

from 1 mm compression molded sheet

DIN 53483, VDE 0303 part 4

E-4

IEC 250, CAMPUS

E-4

0.7

test temperature: 21-25°C; relative plate with dihumidity: 50%; atmosphere accord- mensions 1.0 +/ing to ISO 291 0.1 mm

2.3

2.3 2.3

30

5

dissipation factor at 1 MHz (loss factor)

“

“

“

E-4

2

volume resistivity

“

“

IEC 93, CAMPUS

Ohm*cm

>1E15

>1E15

>1E15

>1E15

1.00E+14

1.00E+14

>1E15

surface resistivity

“

“

“

Ohm

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

dielectric strength

test temperature: 21-25°C; relative humidity: 50%; atmosphere according to ISO 291, short term test in transformer oil according to IEC 296

“

IEC 243-1, CAMPUS

kV/mm

140

30

40

140

40

40

43

>=15 x >=15 x 4 mm

IEC 112, CAMPUS

steps

600

600

600

600

600

dielectric constant at 50 Hz

frequency: 50 Hz

comp. tracking index (CTI)

test temperature: 21-25°C; relative humidity: 50%; atmosphere according to ISO 291, test liquid A


IEC 250


271 polypropylene, polypropylene, polypropylene, polypropylene, polypropylene polypropylene, polypropylene 40% talc 20% glass 20% chemi30% chemiblock block copolyrandom fiber cally coupled cally coupled copolymer mer, UV copolymer glass fibers glass fibers stabilized

polypropylene random copolymer

metallocene polypropylene

metallocene polypropylene, Polypropylene Material family polypropylene elastomerelastomer modified blend recyclate

Hoechst

Hoechst

Hoechst

Hoechst

Vestolen GMBH

BASF

Vestolen GMBH

BASF

Hoechst

Hoechst

Hoechst

Hoechst

Hostacom M4 N01

Hostacom G2 N01

Hostacom G2 U02

Hostacom G3 N01

Vestolen P 7700

Novolen 2660 M

Vestolen P 9421

Novolen 3240 NC

Hostacen XAV10A FOB

Hostacen XAW10A SAB

Hostalen PPN 8018A

Hostalen PP 3100

326, CAMPUS

326, CAMPUS

326, CAMPUS

326, CAMPUS

711, CAMPUS

CAMPUS

711, 712, CAMPUS

756, CAMPUS

709

731

841, CAMPUS

CAMPUS

Supplier Material Trade Name Source ID Test Notes

MECHANICAL PROPERTIES (CONTINUED) 50

40

90

120

3300

2400

4300

5500

62

43

34

20

Ball indentation hardness

34

flexural stress (3.5% strain)

creep modulus (flexure, 1 min value) 1200

flexural modulus

1350

THERMAL PROPERTIES 163 {DTA or DSC; 10°C/min; ISO 3146, CAMPUS} 164-167 {po- 164-167 {po- 164-167 {po- 164-167 {polarizing micro- larizing micro- larizing micro- larizing microscope; 20µm scope; 20µm scope; 20µm scope; 20µm microtome microtome microtome microtome section} section} section} section}

160-164 {DIN 53736 B2}

149 {DTA or DSC; 10°C/min; ISO 3146, CAMPUS} 150-154 {DIN 53736 B2}

150 {DSC}

167 {DTA or melting temperature DSC; 10°C/min; ISO 3146, CAMPUS}

150 {DSC}

crystalline melting range

164-167 {DIN 53736 B2}

125

120

150

155

90

80

65

70

70


75

75

130

140

55

50

45

48

50


92

100

52


153

150

160

160

95

90

125

130

85

58

60

72

0.8

0.8

0.9

0.7

1.5

1.5

1.5

1.85

HB

HB

HB

HB

HB {at 0.8 mm}

HB {at 0.8 mm}

HB

HB

Vicat A softening temperature

130

55

68

Vicat B softening temperature coefficient of linear thermal expansion (flow direction)

HB

flammability UL94 at 1.6 mm flammability UL94 at 1 mm oxygen index

65

generic temperature index

65

0.56 {8 mm 0.25 {8 mm sheet, injection sheet, injection molded} molded}

0.30 {8 mm sheet, injection molded}

0.24

2

1.39

1.53

1.48

1.41

2.9

2.8

2.8

3

2.9

2.8

2.8

3

2.5

2.4

2.4

2.6

50

10

10

10

50

10

10

10

thermal conductivity

0.17

1.7

specific heat

ELECTRICAL PROPERTIES relative permittivity at 50 Hz

2.3

relative permittivity at 100 Hz

2.3 2.3

relative permittivity at 1 MHz

2.3 2.5 {IEC 250}

5

20

0.7

5

2

dissipation factor at 50 Hz (loss factor) dissipation factor at 100 Hz (loss factor)

0.7

2

3.5

dissipation factor at 1 MHz (loss factor)

>1E15

1.00E+14

1.00E+14

1.00E+14

>1E15

>1E15

>1E15

>E15

>E15

volume resistivity

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

1.00E+14

6.00E+11

surface resistivity

40

41

42

40

40

140

35

140

600

600

600

600


600

600

dielectric strength

2.3

dielectric constant at 50 Hz

600

comp. tracking index (CTI)


272

Material family


Supplier

polypropylene polypropylene polypropylene polypropylene, polypropylene, polypropylene, homopolymer, homopolymer, homopolymer, 10% talc 20% talc 20% talc, flame retardant fibers cast film easy-flow

BASF

Vestolen GMBH

Vestolen GMBH

BASF

Hoechst

Hoechst

Hoechst

Material Trade Name

Novolen 1100L

Vestolen P 7006 S

Vestolen P 4000

Novolen 1127 N

Hostacom M1 U01

Hostacom M2 N01

Hostacom M2 U01

Source ID

756, CAMPUS

711, CAMPUS

711, CAMPUS

756, CAMPUS

326, CAMPUS

326, CAMPUS

326, CAMPUS

0.1

0.8

0.8

0.1

2

2

2

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